Bioactive Extraction and Application in Food and Nutraceutical Industries
Bioactive Extraction and Application in Food and Nutraceutical Industries
Bioactive Extraction and Application in Food and Nutraceutical Industries
in Food Science
Bioactive Extraction
and Application
in Food and
Nutraceutical
Industries
METHODS AND PROTOCOLS IN FOOD SCIENCE
Series Editor
Anderson S. Sant’Ana
University of Campinas
Campinas, Brazil
Edited by
Tanmay Sarkar
Dept. of Food Processing Tech, West Bengal State Council of Technical Education, Malda, India
Siddhartha Pati
NatNov Bioscience Private Limited, Odisha, India
Editors
Tanmay Sarkar Siddhartha Pati
Dept. of Food Processing Tech NatNov Bioscience Private Limited
West Bengal State Council of Technical Education Odisha, India
Malda, India
This Humana imprint is published by the registered company Springer Science+Business Media, LLC, part of Springer
Nature.
The registered company address is: 1 New York Plaza, New York, NY 10004, U.S.A.
Methods and Protocols in Food Science series is devoted to the publication of research
protocols and methodologies in all fields of food science. The series is unique as it includes
protocols developed, validated and used by food and related scientists as well as theoretical
basis are provided for each protocol. Aspects related to improvements in the protocols,
adaptations and further developments in the protocols may also be approached.
Methods and Protocols in Food Science series aims to bring the most recent develop-
ments in research protocols in the field as well as very well established methods. As such the
series targets undergraduate, graduate and researchers in the field of food science and
correlated areas. The protocols documented in the series will be highly useful for scientific
inquiries in the field of food sciences, presented in such way that the readers will be able to
reproduce the experiments in a step-by-step style.
Each protocol will be characterized by a brief introductory section, followed by a short
aims section, in which the precise purpose of the protocol is clarified. Then, an in-depth list
of materials and reagents required for employing the protocol is presented, followed by a
comprehensive and step-by-step procedures on how to perform that experiment. The next
section brings the dos and don’ts when carrying out the protocol, followed by the main
pitfalls faced and how to troubleshoot them. Finally, template results will be presented and
their meaning/conclusions addressed.
The Methods and Protocols in Food Science series will fill an important gap, addressing
a common complain of food scientists, regarding the difficulties in repeating experiments
detailed in scientific papers. With this, the series has a potential to become a reference
material in food science laboratories of research centers and universities throughout the
world.
v
Preface
The field of bioactive extraction and its application in the food and nutraceutical industries
has witnessed significant growth and innovation in recent years. Bioactive compounds,
which possess beneficial properties for human health, have garnered attention for their
potential in improving dietary quality and promoting overall well-being. This book, titled
Bioactive Extraction and Application in Food and Nutraceutical Industries, aims to provide
a comprehensive overview of the various aspects of bioactive compound extraction and its
industrial applications.
The chapters in this book cover a wide range of topics, encompassing both traditional
and novel extraction techniques, as well as exploring diverse sources of bioactive com-
pounds. The primary objective is to present a holistic view of the field, catering to the
needs of researchers, industry professionals, and students who are interested in this rapidly
evolving area.
Chapter 1 delves into traditional extraction techniques commonly employed in the
food, nutraceutical, and biotechnology industries. It provides a solid foundation by discuss-
ing the technological advancements and applications of these techniques in extracting
bioactive compounds, enabling readers to grasp the fundamentals of the field.
Chapters 2 and 3 specifically focus on the extraction of bioactive compounds and
nutraceuticals from plants and marine sources, respectively. These chapters shed light on
the wide array of bioresources available and explore the applications of plant-based and
marine-derived compounds in the food and nutraceutical sectors. Readers will gain insights
into the diverse range of bioactive compounds that can be extracted from these sources and
their potential benefits.
The subsequent chapters delve into the application of specific extraction techniques.
Chapter 4 discusses the utilization of microwave-assisted extraction for bioactive com-
pounds, highlighting its efficiency and effectiveness. Chapter 5 explores ultrasound-assisted
extraction, another powerful technique that has gained popularity in the food, pharmacy,
and biotech industries. Both of these chapters present practical insights into these innovative
extraction methods.
Chapters 6 and 7 introduce supercritical and subcritical fluid extraction and novel
solvent-based extraction, respectively. These advanced techniques offer unique advantages
in terms of efficiency, selectivity, and sustainability. The chapters provide comprehensive
coverage of their principles, applications, and potential in the extraction of bioactive
compounds.
Chapter 8 focuses on enzyme-assisted extraction, a promising method that harnesses the
power of enzymes to enhance extraction efficiency. This chapter delves into the enzymatic
hydrolysis of plant and microbial sources and its potential for extracting valuable bioactive
compounds.
Chapter 9 introduces pulsed electric fields as a green technology for the extraction of
bioactive compounds. This emerging technique utilizes electrical pulses to disrupt cell
membranes and facilitate the release of bioactive compounds, offering a sustainable alterna-
tive to traditional extraction methods.
vii
viii Preface
ix
x Contents
Index . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 469
Contributors
xi
xii Contributors
Abstract
The successively growing consumer interest in natural bioactive compounds associated with human health
promotion and disease prevention has received huge attention in the food market toward effective
extraction techniques. Bioactive compounds can be extracted from natural sources and commercially
utilized in the development of nutraceuticals and functional foods. Various novel extraction technologies,
such as supercritical fluid extraction, ultrasound and microwave-assisted extraction, and accelerated solvent
extraction, have been considered effective for large-scale recovery, less extraction time, and superior extract
quality. The choice of an appropriate extraction technique could be based on the final applications or the
process optimization of bioactive compounds. This chapter aims to present conventional and emerging
techniques suitable for extraction of bioactive compounds from natural sources and its potential utilization
in food and nutraceutical industries.
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_1,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
1
2 Rinku Sudarshan Agrawal and Nilesh Prakash Nirmal
Extraction of bioactive
compounds
Purification
(TLC, Column chromatography, HPLC)
Table 1
Advantages and disadvantages of extraction techniques
Supercritical fluid
Maceration
extraction
Ultrasound assisted
Percolation extraction
Microwave assisted
Hydrodistillation extraction
Enzyme assisted
extraction
Pressurized liquied
extraction
3.1 Maceration Maceration, since long, is one of the simplest and inexpensive
techniques widely used for the extraction of essential oil and bioac-
tive compounds from plant material. The whole or coarsely pow-
dered plant material is soaked with a solvent, such as ethanol,
acetone, or hexane, in a closed vessel. This is allowed to stand at
room temperature for 2–3 days with frequent stirring, which facil-
itates extraction. The process is intended to rupture the cell struc-
ture and help in the removal of different plant components. The
mixture is then pressed or strained by filtration or decantation after
a specific time [7]. The extraction efficiency was lowest in the
extracts of the maceration method, and it is a time-consuming
method. But it could be used for the extraction of thermolabile
components.
3.3 Hydro Distillation Hydro distillation is another conventional method that uses water
or steam for the extraction of bioactive compounds, especially
essential oils from plants. Hydro distillation is often carried out
using an equipment known as Clevenger apparatus or simple steam
distillation. In the Clevenger apparatus, sample mixed water is
boiled to evaporate volatile components, while in the steam distil-
lation approach, the steam is passed through a bed of the sample. In
6 Rinku Sudarshan Agrawal and Nilesh Prakash Nirmal
both methods, two layers (aqueous and oil-rich) are obtained and
oil can be further separated via separating funnels [9]. Hydro dis-
tillation consumes more time, high levels of energy distillation rates
may vary if the heat source is not controlled, and the direct heat
source may cause charring of plant material at the base of the
chamber [10].
3.4 Soxhlet Soxhlet extraction is one of the most popular conventional techni-
Extraction ques for extracting valuable bioactive compounds from various
natural sources. This is an automatic continuous extraction tech-
nique having high extraction efficiency that requires less time and
solvent consumption than maceration or percolation. However, it is
widely applied to compounds with high thermal stability [8].
The finely ground material is placed in a thimble-holder made
from cellulose or filter paper and kept in a Soxhlet apparatus.
Extraction solvents are heated in a round bottom flask, vaporized
into the sample thimble, condensed in the condenser, and dripped
back. When the liquid reaches an overflow level, a siphon aspirates
the whole content of the thimble-holder and unloads it back into
the distillation flask, carrying the extracted analytes in the bulk
liquid. This process is continued until complete extraction is
achieved [6]. The efficiency of this process depends on parameters
such as solubility, mass transfer, and solid material characteristics.
The selection of a suitable solvent is one of the most important
factors for the extraction of bioactive compounds since it must be
based on its ability to extract the target compound [11]. This
technique has also been combined with microwave-assisted extrac-
tion and ultrasonic extraction in an attempt to improve extraction
efficiencies.
4.1 Supercritical The supercritical fluid extraction (SFE) technique offers numerous
Fluid Extraction (SFE) operational advantages over conventional methods as it uses super-
critical solvents with various physico-chemical properties. The SFE
technology is extensively adapted for the extraction of thermolabile
biomolecules without any degradation of compounds. It involves
modulation of physical features, such as increasing the temperature
and pressure of a substance or solvent above its critical values. The
changes in fluid density in its supercritical state allow for variation in
solvency power, which results in selective extractions of compounds
of interest [15].
This technique makes use of supercritical fluids such as CO2,
ethanol, and water, which are generally recognized as safe (GRAS)
by the US Food and Drug Administration (FDA). Particularly,
supercritical carbon dioxide (SC-CO2) is extensively used as a
solvent as it is inert, nontoxic, economical, and easily separable
from the final product [8]. SC-CO2 is characterized by low viscos-
ity, high density, and diffusivity than conventional solvents, which
helps to have enhanced transport properties than liquids, diffuses
very easily through solid materials, and thus increases the extraction
rate of compounds [16]. SC-CO2 has unique solvent properties
that make it a desirable compound for separating antioxidants,
essential oils, pigments, flavors, fragrances, and fatty acids from
plant and animal materials. The productivity and profitability of a
supercritical fluid extraction (SFE) process largely depend on the
selection of process parameters.
4.4 Pulsed Electric Pulsed electric field involves the application of high voltage pulses
Field (PEF)-Assisted for a brief time period (nanoseconds/milliseconds) through the
Extraction sample placed between two conducting electrodes [23]. Pulsed
electric fields (PEF)-assisted extraction is attracting great attention
as a nonthermal extraction technology due to being a cost-effective
technique that is energy efficient, time-saving, and eco-friendly
[24]. PEF has proven to be a promising technique to enhance the
extraction of valuable bioactive compounds such as anthocyanin,
polyphenols, and plant oil from plant tissues, as well as their bypro-
ducts and soluble intracellular matter from microorganisms.
The targeted material is placed between the electrodes, and a
high voltage electric field of 10–60 kV is applied through electro-
des. The applied high voltage pulse induces pores in the cell mem-
branes (electroporation), which enhances the permeability of the
cell membrane. The cell membrane loses its structural functionality,
leading to cell disintegration, which accounts for the leakage of
intracellular content, and the plant material is extracted [25]. PEF
has the ability to electroporate the cell membranes and is thus
commonly used as pretreatment to facilitate the extraction of bio-
active compounds, followed by subsequent conventional or
advanced extraction techniques [11]. This technique is usually
preferred for liquid foods as electrical current flows into the liquid
food more fast and effectively and the transfer of pulses from one
point to another in liquids is quite easy due to the presence of
charged molecules [26].
Numerous studies concluded PEF as a promising tool to
recover phytonutrients used in the food and pharmaceutical indus-
tries. PEF-assisted extraction leads to cost efficiency, higher extract
yield of bioactive compounds, lower energy consumption, and less
treatment time, providing the optimum process parameters. The
extraction efficiency of bio ingredients with PEF treatment depends
on electrical parameters such as electric field strength, energy input,
pulse polarity, and delay time between pulses of opposite polarity.
4.6 Pressurized Pressurized liquids are able to recover phytonutrients faster than
Liquid Extraction (PLE) conventional low pressure methods. PLE can be viewed as an
extension of supercritical fluid extraction, utilizing organic solvents
instead of carbon dioxide. PLE uses liquid solvents below their
critical point with controlled temperature and pressure [30]. PLE
was first introduced as accelerated solvent extraction (ASE) tech-
nology in 1995 by Dionex Corporation as an alternative to other
Technologies for Extraction of Bioactive Compounds and Its Applications 11
Table 2
Bioactive compounds from fruit and vegetable processing waste and by-products
8.1 Functional Foods The successively growing demand for foods with beneficial effects
on human health, while contributing to the sustainable use of
natural resources, enhances the research interest in potential utili-
zation of bioactive compounds. Bioactive compounds are receiving
more popularity due to their diverse biological activities and huge
exploitation in various commercial sectors, such as food,
pharmaceutical, and cosmetic industries. These compounds exhibit
beneficial effects such as antioxidant activity, anti-diabetic, anti-
cancerous, antidiuretic, anti-atherosclerotic, and so on for human
beings. Bioactive compounds have multiple applications in food,
acting as antimicrobials, antioxidants, natural dyes, fortifying ingre-
dients, texture modifiers, and others [58]. Bioactive ingredients
such as anthocyanins, curcumins, tannins, and carotenoids are
commonly applied as natural colorings in food product prepara-
tions [59]. Moreover, they have also been used for the develop-
ment of active and smart biodegradable food packaging
materials [60].
The technological advancements made possible the extraction
of bioactive compounds not only from natural sources but also
from byproducts and their reintroduction into foods. Bioactive
compounds can be used to improve the quality of conventional
foods with respect to nutritional, sensorial, and technological prop-
erties (e.g., water and oil holding capacities, foaming, emulsion,
and gelatinization) [61]. Bioactive compounds are key factors in
the development of nutraceuticals and functional foods. The possi-
bility of applying bioactive components in food products and in
new technologies to enhance food product quality and safety is
enormous. Due to the diversity of compounds, their possible inter-
actions, and various physiological activities, each component must
be properly evaluated for the production of food, beverages, and
active and smart packaging applied to food to guarantee maximum
potential in the applications [45].
8.2 Food Phenolic compounds are well known for their health benefits
Preservatives related to antioxidant activity and thus have potential use as bio-
preservatives. These compounds are extensively studied for their
potential application in the food sector for improving the shelf life
of perishable food products. The biological activity of phenolic
compounds delays or inhibits the oxidation and growth of micro-
organisms; these compunds are thus considered as biopreservatives
for safe extension of perishable products [62].
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20 Rinku Sudarshan Agrawal and Nilesh Prakash Nirmal
Abstract
Natural bioactive compounds are a useful source of molecules for the development of nutraceuticals, food
additives, and functional foods because they contain a wide variety of diverse structural and functional
properties. Although extracting them for use in biological and/or phytochemical investigations presents
some particular challenges, plant-derived bioactive and nutraceutical compounds are now the subject of a
lot of studies since they offer a variety of biological properties and therapeutic benefits. In order to cut costs
related to their synthesis and separation, the process of extracting active phytochemicals is also carefully
taken into account. Despite the fact that natural bioactive compounds and functional foods have been used
as traditional medicines to treat chronic diseases for decades, recent scientific studies emphasize the health
advantages of functional meals and reveal the underlying processes that underlie their activities. To cure and
prevent inflammatory and oxidative diseases, phytochemicals perform essential bioactive roles. Plant-
derived bioactive compounds that don’t cause oxidative damage and interact with the immune system
might lessen inflammation. The capacity to bind to poisons or carcinogens that impact the digestive system
exists in many bioactive compounds.
This chapter’s goal is to present, summarize, and assess the many approaches utilized to extract bioactive
and nutritional components from plants, besides their most recent applications.
1 Introduction
Herbal items made from medicinal plants are useful sources that
come from all over the world and can include a wide range of
ingredients [1, 2]. Natural remedies have been used to cure both
acute and chronic illnesses [3] for as long as human civilization has
existed. One of the most significant sources of food and medicine
for people is natural products [4]. They often contain a range of
physiologically active chemicals, such as phenolic substances, vita-
mins, sulfur compounds, pigments, terpenoids, and other naturally
occurring antioxidants [5], which are efficient in enhancing defense
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_2,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
21
22 Hadia Hemmami et al.
3 Bioactive Compounds
N
N
CH3 OH
N
OH O OH
OH
HO O
CH3 CH3
O O
O
OH
Polyacetylenes Sesqueterpenes
Polyketides
OH
C O HO O
OH
OH
OH
RO
OH O
Fig. 4 Steps involved in extraction, isolation, and characterization of bioactive compounds from plant extract
5.1 Extraction The primary step in analyzing important plant components for
Methodology separation and characterization is extraction.
Prewashing, drying plant materials in the air, obtaining a
homogeneous sample by grinding, and often enhancing the kinet-
ics of extract by increasing sample contact with the solvent system
are the most crucial processes. The proper steps must be followed
to prevent possible active extract ingredients from being distorted
or destroyed during sample preparation. If the plants are chosen
based on their traditional usage [45], plant sample extracts are
made according to the traditional healer’s instructions in the same
sequence to mimic the traditional “herbal” medication as closely as
feasible. The clear-cut nature of the bioactive compounds being
targeted is a major factor in the solvent system selection. For
instance, the hydroalcoholic leaf extract of Aegle marmelos was
found to be effective against MNU-induced toxicity, which is
responsible for liver inflammation and hepatocarcinogenesis
[46]. There are several extraction solvent systems available to
extract the bioactive components from natural goods. Polar sol-
vents like methanol, ethanol, or ethyl acetate are used to isolate
hydrophilic chemicals, whereas dichloromethane or a 1:1 combina-
tion of dichloromethane and methanol is utilized to isolate more
hydrophobic compounds.
28 Hadia Hemmami et al.
5.2 Identification Modern methods allow for the concurrent creation of several com-
and Characterization plex bioassays and their accessibility, while also offering precise
methods for isolation, separation, and purification [49]. The objec-
tive of searching for bioactive chemicals is to find a method that is
suitable for monitoring the source material for bioactivity, such as
antibacterial, cytotoxicity, or antioxidant, with simplicity, specific-
ity, and speed (Fig. 5) [50]. Due to the expense, length of time, and
potential for ethical problems associated with animal research,
in vitro procedures are typically more favorable than in vivo trials.
Although diverse plant sections and/or many of them will create
different chemicals, in addition to their varying chemical structures
and physicochemical qualities, the isolation and characterization
techniques for bioactive compounds are not difficult [51]. The
5.3 Purification of Paper or TLC and column chromatography have been used to
the Bioactive identify and characterize a large number of bioactive chemicals.
Molecules Due to their accessibility, affordability, and ease in a variety of
stationary phases, TLC and column chromatography are still fre-
quently utilized. The most effective methods for separating the
phytochemicals may be found in silica, alumina, cellulose, and
polyamide.
30 Hadia Hemmami et al.
5.3.1 UV-Visible UV-visible spectroscopy may be used for qualitative analysis and the
Spectroscopy (UV-Vis) identification of certain types of compounds in both pure and
biological mixtures. Quantitative research on aromatic chemicals
uses UV-visible spectroscopy because they are potent UV chromo-
phores. Natural chemicals can be identified via UV-visible spectros-
copy [56]. Anthocyanidins, tannins, polymer dyes, and phenols are
phenolic chemicals that may be easily identified by UV-Vis spec-
troscopy [57]. It was discovered that UV-Vis methods are less
discriminating and provide complicated data on total polyphenol
content. The total phenolic extract (280 nm), phenolic acids
(360 nm), flavones (320 nm), and anthocyanidins are all quantified
using UV-Vis spectra (520 nm). Comparing this procedure to
others, it is both less time- and money-consuming [57].
5.3.2 Infrared When infrared light passes through a sample of an organic mole-
Spectroscopy (IR) cule, some of the frequencies will be absorbed while other frequen-
cies will pass through the sample undetected. When a molecule is
exposed to infrared light, it undergoes changes in vibration that are
related to infrared absorption. As a result, it is possible to think of
infrared spectroscopy as a type of vibrational spectroscopy. The
vibrational frequencies of various bonds (C-C, C=C, CC, C-O,
C=O, O-H, and N-H) vary [56]. By identifying the distinctive
frequency absorption band in the IR spectra, it is possible to deter-
mine if such bonds are present in an organic molecule [10]. A high-
resolution analytical technology called Fourier Transform Infrared
Spectroscopy (FTIR) is used to pinpoint the chemical components
and clarify the structural compounds. Herbal extracts or powders
can be quickly and nondestructively fingerprinted using FTIR.
Extraction of Bioactive and Nutraceuticals from Plants and Their Application 31
5.3.3 Fourier Transforms Infrared spectroscopy using the Fourier transform is a useful tech-
Infrared Spectroscopy nique for locating functional groups in plant extracts. It aids in
(FTIR) molecular identification and structural determination. It is a high-
resolution analytical instrument for deciphering structural com-
pounds and identifying chemical ingredients. Herbal extracts or
powders may be quickly and nondestructively fingerprinted using
FTIR [58]. The spectrum of an unknown molecule can be identi-
fied by comparison with a known compound spectra for the major-
ity of typical plant compounds. There are several ways to prepare
samples for this method. The easiest method for liquid samples is to
sandwich one drop of the sample between two plates of sodium
chloride. Between the plates, the drop creates a thin layer. Potas-
sium bromide (KBr) may be used to crush solid materials, and the
resulting thin pellet can subsequently be examined. Another
method for solid samples is to first dissolve the preparation in a
solvent system, such as methylene chloride, and then transfer the
resulting solution to a single salt plate. A thin coating of the original
material is then formed on the plate once the solvent has evapo-
rated. FTIR is a high-resolution analytical method used to reveal
the structure of compounds and identify the chemical constituents.
Herbal extracts or powders can be quickly and nondestructively
analyzed using FTIR [59].
5.3.4 Nuclear Magnetic The magnetic properties of atomic nuclei, notably those of the
Resonance hydrogen atom, proton, carbon, and an isotope of carbon, are the
Spectroscopy (NMR) primary focus of NMR. By comparing the differences between a
variety of magnetic nuclei, which gives a clear image of where these
nuclei are positioned in the molecule, NMR spectroscopy has
enabled numerous researchers to investigate molecules. It also
shows which atoms are present in the clusters that are close
by. Finally, it can be argued that a lot of atoms are present in each
of these settings [57, 60].
5.3.5 Identification of In mass spectrometry (MS), molecules are attacked with a mixture
Chemical Compounds of electrons or lasers before being changed into charged ions, which
Using Mass Spectrometry have a high energy. A mass spectrum is a graph that shows how
many fragmented ions there are in relation to their mass/charge
ratio. By using MS, using information about the areas where the
molecule has been split apart, it is feasible to calculate the relative
molecular mass (molecular weight) with high precision and con-
struct a precise molecular formula [61]. The most significant and
popular advanced technology is tandem mass spectrometry
(MS/MS). In addition to increasing selectivity, MS/MS offers a
plethora of structural data, enabling the identification and measure-
ment of even co-eluting molecules [62]. For the first time, the
phenolic compounds quercetin, crysin, quinic acid, chlorogenic
acid, and kaempferol were successfully screened and identified in a
32 Hadia Hemmami et al.
5.3.6 Nonchromato- Research on receptor binding analysis, enzyme assay, and quantita-
graphic Techniques tive and/or qualitative analytical procedures in animals or plants has
made monoclonal antibody (MAb) against drugs and tiny molecu-
lar weight bioactive chemicals an indispensable tool. The immuno-
blotting approach is based on the western blotting method, which
makes use of the antigen-antibody binding capabilities to identify
larger molecule analytes like peptides and proteins in a precise and
sensitive manner. ELISA, a highly sensitive, precise, and easy-to-use
technology, was created for individual competitive testing
[64]. Since their introduction, monoclonal antibodies (MAbs),
which have a wide range of applications, have grown in significance
as a tool in contemporary bioscience research. Recently, several
researchers have concentrated on the creation of MAbs against
the secondary metabolites, or natural compounds, obtained from
medicinal plants [65].
The procedures used to create monoclonal antibodies using
hybridoma technology against plant-based medications are as
follows:
(i) Adequate purification and characterization of the required
antigen.
(ii) Giving mice an immunity boost using the purified antigen.
(iii) The cultivation of myeloma cells that are unable to produce
the hypoxanthine-guanine-phosphoribosyl transferase
(HGPRT) enzyme required for the nucleic acid salvage
pathway.
(iv) The removal of mouse spleen cells and their fusion with mye-
loma cells.
(v) The hybridomas were raised in hypoxanthine aminopterin
thymidine (HAT) medium after fusion [66].
6.1 Use of Natural Bioactive food components are essential in both the prevention and
Bioactive Compounds treatment of diseases since various chemicals are involved in the
in the Food and pathophysiology of many disease processes. Several bioactive che-
Pharmaceutical micals actively control the inflammatory process, which is the
Industries underlying cause of diabetes, cancer, and other inflammatory dis-
eases. Dietary practices, food components, and bioactive substances
with anti-inflammatory characteristics have all been found to be
protective. Utilizing bioactive food substances with antioxidant
and anti-inflammatory characteristics that are found in spices and
herbs may thus help avoid inflammation that can lead to carcino-
genesis or cardiovascular disorders [70]. For instance, the two most
successful nonpharmaceutical therapies for inflammatory bowel
disease are dietary changes and functional diets (IBD). IBD can
be treated with probiotics and nonstarchy polysaccharide dietary
supplements. Omega-3 fatty acids, vitamins, phytochemicals, and
plant extracts are a few examples of bioactive compounds. These
dietary peptides and functional foods have potent anti-
inflammatory effects in both human and animal studies [71]. In
order to reduce inflammation, functional foods can alter inflamma-
tory cytokines and work with the immune system. The manufacture
of nutraceuticals for inflammatory-related disorders is made possi-
ble by the anti-oxidative and anti-inflammatory action of cotonea-
ster’s polyphenolic components [72]. Angiotensin-converting
enzyme (ACE) inhibitors, which are bioactive components of Cor-
iandrum sativum, are thought to have anti-hypertensive
effects [73].
Plant-derived phytochemicals offer a promising new route for
the creation of diabetic mellitus therapies. The more significant
alkaloids include flavonoids, glycosides, terpenoids, and steroids
[74]. Numerous phytochemicals with possible antidiabetic
34 Hadia Hemmami et al.
6.2 Use of Bio-Based The Product and Drug Administration (FDA) defines “natural” as
Compounds as Food a food that “does not include anything artificial or synthetic,
Additives including additives,” despite the fact that the phrase has no legal
definition. Due to studies indicating negative impacts of the usage
of synthetic ingredients, there has been an increase in research and
demand for natural foods during the past few years. Additionally,
the phrase “natural” adds value to the product because it is now
fashionable to consume goods made entirely of natural substances
[88, 89].
Because they include chemicals that are good for health, plants,
fruits, and spices are well known. The biologically active com-
pounds found in plants that are used as food additives can be
unofficially categorized as antioxidants, antimicrobials, flavorings,
colorants, and others. More research has been done as a result of
increased public awareness of the benefits of ingesting natural
goods, leading to potential sources of natural additives [90].
There are a ton of raw materials with a high concentration of
bioactive compounds in the by-products and biowaste from the
food sector. For instance, orange peels may be used as flavorings,
sweeteners, and antioxidants since they include essential oils, cellu-
lose, pectin, hemicellulose, and soluble sugars (galactose, sucrose,
fructose, and glucose) [91].
The utilization of vegetable byproducts and bio-residues is an
alternative to synthetic additives since consumers are more inter-
ested in additives derived from natural sources and have a sustain-
able mentality [92].
from A. esculentus flowers, was studied by Y. Luo et al. [94] for its
potential protective effects on TCI-RI. The researchers demon-
strated that AFF had protective effects against TCI-RI by scaveng-
ing free radicals and indirectly boosting the neuronal Nrf2-ARE
pathway to reduce oxidative stress damage.
Alzheimer’s disease (AD) is a neurodegenerative illness of the
central nervous system that gradually impairs cognition and mem-
ory. The disease’s molecular characteristics include extracellular
amyloid peptide (A) deposition in senile plaques, the emergence
of intracellular neurofibrillary tangles (NFT), cholinergic deficit,
significant neuronal loss, and synaptic alterations in the cerebral
cortex, hippocampus, and other brain regions crucial for cognitive
and memory functions. A deposition kills neurons by a number of
different possible mechanisms, including oxidative stress, excito-
toxicity, energy depletion, inflammation, and apoptosis [95].
A member of the Caryocaraceae family known as “pequi,”
Caryocar brasiliense (Camb), is one of the promising neuroprotec-
tive phytomedicines. In their article, “Neuroprotective Effect of
Caryocar brasiliense Camb.,” T. S. de Oliveira et al. [86] investi-
gated the antioxidant and anticholinesterase activities as well as the
neuroprotective effects of C. brasiliense leaf extracts to provide new
information on the potential use of this plant against neurodegen-
erative disorders.
Memory loss that worsens over time, along with other cogni-
tive impairments, are common AD symptoms. The amyloid
hypothesis states that synaptic malfunction and consequent neuro-
degeneration in AD are primarily caused by amyloid- (A-) asso-
ciated toxicity and imbalance. A has been proposed as a possible
therapeutic target for the treatment of AD as a result. Procyanidins
extracted from Lotus seedpod ameliorate amyloid—induced
toxicity in rat Pheochromocytoma cells [96] study by H. Huang
et al. confirms the anti-A activities and protective mechanisms as a
potential natural product for AD therapy. The authors assessed the
LSPC’s ability to mitigate the harm caused by A-25-35 to rat
pheochromocytoma (PC12) cells.
In the case of infection, inflammation, trauma, ischemia, and
neurodegeneration in the central nervous system (CNS), microglia
cells act as scavenger cells and play a crucial function as resident
immunocompetent and phagocytic cells [97]. While prolonged
activation of microglia and astrocytes causes neuroinflammation,
which can start or accelerate dementia, it is a brain defense system
to combat dangerous infections and damaged tissues [98].
Numerous herbal plants and their active ingredients have sur-
faced in recent years and have been the focus of in-depth study.
When opposed to contemporary trendy supplements, these medi-
cines have been time-tested and verified by traditional usage.
Recent research has shown that traditional herbal remedies with
reliable ethnopharmacological qualities have neurotrophic and
Extraction of Bioactive and Nutraceuticals from Plants and Their Application 37
7 Future Perspectives
Due to the fact that there are still 500,000 plants in the world that
need to be found, examined, and investigated by the scientific
community for their potential therapeutic capabilities to treat a
variety of ailments, bioactive chemicals and herbal medications
have a bright future. Worldwide demand for items made from
plants has expanded, yet traditional indigenous medical methods
are still in their infancy. For the treatment and healing of a wide
range of ailments, herbal compositions and diverse formulations
have been used for many generations with careful selection and
application [105]. For their medical requirements, almost 85% of
the population in Asia, Africa, Latin America, and the Middle East
largely trust traditional herbal remedies. Skin conditions, jaundice,
cancer, TB, hypertension, diabetes, and many other infectious dis-
orders are successfully treated using bioactive chemicals and their
analogs at both the chronic and acute levels [106]. These bioactive
compounds do, however, have some disadvantages, including
changes in composition with climate, the concurrent occurrence
of synergistic effects of compounds, their mode of administration,
and stability in active form, which may have unfavorable or unex-
pectedly positive effects on bioactivity. These problems can be
resolved by utilizing state-of-the-art techniques for the isolation
of pure bioactive compounds, their synthesis as herbal nanoparti-
cles, and convenient examination of their therapeutic effects in
addition to toxicity analysis prior to medication after keeping the
extract for longer periods of time [107]. A. aspera leaf extract was
characterized using MALDI-TOF-MS, which reveals the presence
of chlorogenic acid (CGA). The extract was also utilized to create
herbal gold nanoparticles, and fresh splenocyte cell culture was
38 Hadia Hemmami et al.
8 Conclusions
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Chapter 3
Abstract
The marine resource hosts wide biodiversity, regarded as a rich source of diverse bioactive compounds,
which are widely investigated for their bioactive composition and nutraceutical applications having several
health benefits. Several in vitro and in vivo studies have reported the impacts of marine bioactive com-
pounds in controlling several lifestyle disorders. Based on their high bioactive compounds and nutraceutical
value, their extraction techniques are known to influence their bioactivity widely. The present chapter
summarizes the knowledge on novel extraction technologies of bioactive compounds from marine sources;
further, based on their bioactivity and nutraceutical property, their ability to modulate development of
several disorders is addressed. Besides, the chapter covers food application of derived bioactive compounds
to develop nutraceutical foods.
1 Introduction
Oceans are habitat to the most diverse plants and creatures on the
planet. Marine organisms (planktons, seaweeds, microalgae,
microbes, invertebrates, fish, and so on) have been discovered to
be a potential source of numerous bioactive and nutraceutical
compounds [1, 2]. The compounds exhibit a wide range of func-
tional characteristics, including antioxidant, anti-inflammatory,
anti-microbial, anti-hypertensive, anti-cancer, neuroprotective,
and so on. In an animal model, consumption of seaweed potentially
ameliorates conditions associated with chronic diseases such as
cardiovascular diseases, hyperlipidaemia, diabetes, obesity, and
hypertension [3, 4] through modulation of various signaling
pathways. The major marine-sourced phytochemicals with health-
protective effects are phenolics, flavonoids, terpenoids,
phytosterols, and alkaloids [5]. In addition to phytochemicals,
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_3,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
45
46 Nikheel Rathod et al.
2.4 Supercritical CO2 It uses solvents at supercritical temperature and pressure condi-
Extraction tions, exhibiting properties of between a liquid and a gas, helping
in improved extraction of bioactive compounds [31]. Considering
the low critical conditions and higher diffusivity of carbon dioxide
(30 °C and 7.38 MPa), it is used for recovery of target compounds.
The proper relation between the pressure and temperature can be
so managed to ensure extraction of heat-labile compounds
[32]. The major advantage of using this technique is reduced
usage of toxic organic solvents. The low polarity of carbon dioxide
limits the extraction of nonpolar compounds. Hence, compounds
are used to modify the polarity ensuring improved salvation
capacity.
50 Nikheel Rathod et al.
3.1 Bioactivity Antioxidants are used to lessen oxidative damage to the human
body and to extend the shelf life of lipid-containing foods and
3.1.1 Antioxidant
maintain their nutritious content. They also work to prevent dam-
Property
age caused by free radicals. In contrast to naturally occurring anti-
oxidants such tocopherol, ascorbate, and carotenoids, synthetic
antioxidants like butylated hydroxy anisole (BHA), tertiary-butyl-
hydroquinone (TBHQ), and butylated hydroxytoluene (BHT) are
also available. Natural antioxidants from marine sources, such as
protein hydrolysates, peptides, and amino acids, are increasingly
Extraction of Bioactive and Nutraceuticals from Marine Sources. . . 51
Table 1
Bioactive compounds from marine sources and their activities
(continued)
Extraction of Bioactive and Nutraceuticals from Marine Sources. . . 53
Table 1
(continued)
just a few of the algae that have been identified as excellent sources
of phycobiliproteins. These pigments have been found to have
antioxidant capabilities, according to a recent study by Menaa and
others [44]. Carrageenans derived from Hypnea spp. exhibit anti-
oxidant characteristics and hypocholesterolemic effects by lowering
cholesterol and sodium absorption while increasing potassium
absorption [60]. The complex sulfated polysaccharide, known as
porphyran, which is derived from red Porphyra spp., possesses
immunoregulatory, antioxidant, and anticancer properties
[44]. Sargassum thunbergi, Ascophyllum nodosum, Viz fucusvesicu-
losus, Laminaria japonica, Fucusevanescens, and Laminaria cichor-
ioides are a few examples of brown algae that contain fucoidans,
which have antioxidant properties [44].
The antioxidant properties of sulfated polysaccharides isolated
from Monostromaangicava are correlated with the degree of sulfa-
tion and a moderate molecular weight [43]. A powerful antioxi-
dant, iodine is present in most edible seaweeds [44]. The water-
soluble vitamins thiamine, riboflavin, niacin, pantothenic acid, and
biotin, as well as the fat-soluble vitamins retinoic acid and toco-
pherols with antioxidant properties, are both abundant in
seaweeds [44].
3.1.2 Antimicrobial Food antimicrobials are used to stop the development of germs that
Property lead to food spoiling. The most widely used antimicrobial medica-
tions are organic acids (sorbic acid, acetic acid, citric acid, etc.),
which alter the permeability of cell membranes to substrates and
create pH conditions that are unfavorable to bacterial development.
Despite being a very effective preservative, organic acids like sorbic
acid are known to break down when exposed to water and generate
potentially dangerous compounds like acetaldehyde. Ethyl acetate
was used as the extraction solvent to produce an extract from the
edible abalone species Haliotistuberculata coccinea, sometimes
54 Nikheel Rathod et al.
3.1.3 Antihypertensive Different marine fish and fish body parts, such as those from tuna,
Property yellowfin sole, scad, Hoki, Pacific hake, yellow stripe trevally, and
conger eel, have been used to make peptides (fish bones, muscles,
skin, intestines, etc.). Peptides from fish have been found to have
antihypertensive effects [64]. The production of Angiotensin-
converting enzyme inhibitory peptides is influenced by the hydro-
lysis circumstances, substrate protein, and peptidase type.
Extraction of Bioactive and Nutraceuticals from Marine Sources. . . 55
3.1.4 Anticancer The world’s population has been impacted by cancer as a significant
Property cause of mortality in both direct and indirect ways. Although cancer
cases are on the rise, some of them may be avoidable or even
treatable by using natural substances. The risk of chronic diseases
is said to be reduced and overall health is maintained by bioactive
peptides that can be found on land and in the water. Fish bypro-
ducts are a source of bioactive peptides and may be anticarcinogenic
[66]. Anticarcinogenic peptides inhibit the growth of cancer cells in
a number of different methods, such as (1) in the cytoplasm, (2) by
promoting membrane rupture through micellization, and (3) by
interacting with cells during apoptosis via gangliosides on the
surface. Anticancer properties were found in peptides made from
leftover fish processing raw material [62].
Cytotoxicity is the most frequent biological characteristic of sea
cucumber glycosides, making them one of the most researched
anticancer drugs. To present, a variety of sea cucumber species
have produced more than 300 triterpene glycosides with notable
pharmacological characteristics. Argusides A–E, triterpene glyco-
sides derived from Bohadschiaargus, have exhibited significant
in vitro cytotoxicity against a number of human carcinoma cell
lines. Against six different tumor cell lines (P-388, A-549,
MCF-7, MKN-28, HCT-116, and U87MG), the triterpene glyco-
sides, pentactasides I–III, as well as philinopsides A–B, isolated
from Pentactaquadrangularis elicited a remarkable in vitro cyto-
toxicity effect with an IC50 value ranging from 0.60 to 3.95 M. In
56 Nikheel Rathod et al.
3.1.5 Anticoagulant A series of events take place during blood coagulation that, if
Property unchecked, might result in coronary artery blockage. During plate-
let activation, a large number of platelets gather. Next, prothrom-
bin is changed into thrombin, a serine protease that turns soluble
fibrinogen into its insoluble form, fibrin. As more thrombin is
produced, the conversion of fibrinogen to fibrin is enhanced. The
combined effects of vasoconstriction and obstruction of coronary
arteries by fibrin complex formation within the blood vessel result
in myocardial ischemia and heart attacks. Limiting platelet aggre-
gation will thereby reduce vasoconstriction and the risk of myocar-
dial ischemia in these circumstances. The king of physiologically
active chemicals, fucoidan is a highly branched, diverse monosac-
charide with a high molecular weight (10,000–100,000 Da). The
complex chemical structure promotes its anticoagulant
potential [52].
The molecular weight of fucoidans and the amount of galac-
tose they contain both affect the seaweeds’ ability to prevent clot-
ting. Four of the seven fucoidans isolated from the seaweed
Saccharina japonica (Ochrophyta, Phaeophyceae) differ in both
average molecular weight and the ratio of fucose to galactose.
These fucoidans’ results from the activated partial thromboplastin
time (APTT) assay demonstrate that larger molecular weight fucoi-
dans have strong anticoagulant activity, which further raises the
galactose concentration [53]. Sulfated polysaccharides from the
brown seaweed Sargassum fulvellum also showed substantial anti-
coagulant action in the APTT assay, as did several fucans isolated
from the brown algae Padina gymnospora. The APPT test demon-
strated that six families of sulfated polysaccharides from the marine
Extraction of Bioactive and Nutraceuticals from Marine Sources. . . 57
3.1.6 Wound Healing The process of healing a wound involves a number of steps, includ-
Property ing cell migration and proliferation as well as the production of new
extracellular matrix. Brown algal polysaccharide laminarin has a
small molecular weight (MW; 5 kDa). Laminaria and Saccharina
species as well as some Ascophyllum and Fucus species contain
it. Laminarin is made up of sβ-(1,6)-intrachain linkages and (1,3)-
β-D-glucan. Laminarin from Cystoseirabarbata (5% cream) greatly
accelerated reepithelization, increased wound contraction, and per-
mitted restitution of mice skin tissue during the in vivo healing
process [55]. Alginate is a linear polysaccharide made up of consec-
utive block structures of (1–4-)linked β-D-mannuronic acid
(M) and α -L-guluronic acid (G) monomers. The cell wall of
brown macroalgae contains it naturally. Alginates have use in mate-
rials for dental impressions and alginate fiber wound dressings [56].
Carrageenan is a sulfated polysaccharide with a high molecular
weight that is a structural component of the cell membranes of red
macroalgae. It is made up of alternating linear chains of
α-1,3-galactose and β-1,4,3,6-anhydrogalactose with ester sul-
phates (15–40%). Carrageenan is used in the transport of drugs,
the regeneration of bone and cartilage tissue, and wound healing
due to its physiochemical characteristics and gelling mechanism
[72]. Additionally, gelatin is produced into sterile sponges for use
in medical and dental operations, as well as a material for treating
wounds [73]. Oral administration of peptides from different fish
species and their byproducts, like collagen hydrolysates, shows
moisture retention across the face in addition to improved visco-
elastic characteristics and decreased sebum levels. Enzymatic pro-
tein hydrolysates made from the silver carp’s bones and isolated
peptides were more effective at promoting keratinocyte metabolism
and wound healing processes, highlighting the potential of bone
peptides for treating wounds in the cutaneous region [74].
3.1.7 Neuroprotective There has been a significant increase in research on marine micro-
Property bial pigments in recent years. Pigments are molecular structures
that can absorb specific wavelengths of light and reflect the rest of
the visible spectrum. Pigment production by marine bacteria is
thought to be mediated by a quorum-sensing mechanism [75]. Car-
otenes, which are pure hydrocarbon carotenoids without any sub-
stituents in their structures, and xanthophylls, which are molecules
containing oxygen, are the two main categories of carotenoids
Extraction of Bioactive and Nutraceuticals from Marine Sources. . . 59
3.2 Nutraceutical The marine ecosystem is so diverse that it presents a great pool for
Property obtaining new compounds that are beneficial for health improve-
ment and can potentially be used in food, supplement, or therapeu-
tic industries [86]. Thus, newly identified or isolated compounds
from marine sources that carry nutraceutical properties have been
intensively researched in recent years. Marine-origin nutraceuticals
include polysaccharides, peptides and proteins, polyunsaturated
fatty acids (PUFAs), and other lipids, pigments, enzymes, phenolic
compounds, minerals, and vitamins (Fig. 1) [86–88]. The sources
from which these compounds have been isolated include seaweeds
[89], microalgae [90], fish, and a large group of marine inverte-
brates (arthropods, echinoderms, sponges, mollusks, cnidarians,
lophophorates, marine worms, and the hemichordates) [91, 92].
Sulfated polysaccharides found in seaweeds are the most stud-
ied group due to their biological activities. They have shown antic-
arcinogenic, anti-inflammatory, antioxidant, antiviral, and
anticoagulant properties [89, 93]. Polysaccharides make up more
than 80% of the seaweed weight; they serve as structural com-
pounds and energy reserves. The main sulfated polysaccharides
isolated from brown seaweeds are fucoidan, laminarin, and alginate;
from red seaweeds is carrageenan; and from green seaweeds ulvan
[86]. Microalgal polysaccharides also exhibit various biological
activities; also they are components of the microalgal cell wall,
energy reservoirs and serve as cell protection. They are mainly
composed of pentose and hexose monosaccharides with glycosidic
linkage [94]. Marine invertebrates, such as sea cucumbers, asci-
dians, sea urchins, and nudibranchs, are also the source of
Extraction of Bioactive and Nutraceuticals from Marine Sources. . . 61
have a lower lipid content than fish, but they have a high content of
PUFAs and could therefore be a potential alternative source for
their extraction [111, 112].
The main natural pigments isolated from marine sources are
chlorophylls, carotenoids, and phycobiliproteins, which have health
benefits due to their antioxidant, anti-inflammatory, anti-obesity,
antiangiogenic, anticancer, and wound healing properties
[101, 113]. Chlorophylls are synthesized by cyanobacteria and
algae and are mainly responsible for photosynthesis. Apart from
their potential use as substitutes for synthetic pigments in the food
industry, chlorophylls exert antioxidant, antibacterial, anti-
inflammatory, and antimutagenic activities, which make them
potential nutraceuticals [86, 101]. Promising marine sources for
the extraction of chlorophylls are microalgae [114]. The most
abundant carotenoids found in marine sources are fucoxanthin,
astaxanthin, lutein, zeaxanthin, neoxanthin, violaxanthin, and can-
thaxanthin [101]. Astaxanthin and fucoxanthin are the most abun-
dant carotenoids in seaweeds and microalgae [115]. Some fish
species, such as families of Salmonidae and Mullidae, are a good
source of astaxanthin, β-carotene, zeaxanthin, and canthaxanthin
[91], while crustaceans and their byproduct are a valuable source of
natural astaxanthin [78]. Carotenoids found in sponges, jellyfish,
mollusks, crustaceans, sea urchins, and tunicates come from their
diet, and in the case of sponges are also associated with their
symbionts [116]. Carotenoids exhibit various biological activities,
such as antioxidant, anti-inflammatory, anticancer, anti-obesity,
anti-diabetic, wound healing, and photoprotective activities,
which are the foundation for their beneficial effects on health
through the reduction of cardiovascular diseases and cancer risks,
atherosclerosis, non-communicable diseases, and macular degener-
ation [86, 101]. Phycobiliproteins are found in red seaweeds and
cyanobacteria and exhibit antioxidant properties. Research on their
extraction and bioactivity is increasing [117, 118].
Phenolic compounds are a large group of phytochemicals that
have recently gained attention because of their bioactivities and
health-promoting benefits, including antioxidant, antimicrobial,
anti-inflammatory, anti-tumor, anti-allergic, anti-hypertensive,
anti-cholesterol, antithrombotic, anti-diabetic, immunomodula-
tory, wound healing, neuroprotector, photoprotector, and algicidal
properties [119, 120]. This group of compounds can be divided
into simple phenols, benzoic acid derivatives, flavonoids, tannins,
stilbenes, lignins, and lignans. Marine sources of phenolic com-
pounds are microalgae and seaweeds. These organisms produce
them for protection against oxidative stress, biofouling, predators,
pathogens, and other external factors [101, 119, 121]. Among the
three groups of seaweeds, brown algae have been known to yield
more phenolic compounds [119, 122, 123].
Extraction of Bioactive and Nutraceuticals from Marine Sources. . . 63
Bioactive molecules
or nutraceuticals Marine source Food application Main findings References
Astaxanthin Pink deep-water shrimp Marinated chicken Natural astaxanthin was effective as vitamin C in [133]
(Parapenaeuslongirostris) by-products steaks preventing lipid oxidation of marinated
(heads, cephalothorax and appendices) chicken steaks
Texture of samples was improved
Nikheel Rathod et al.
(continued)
65
66
Table 2
(continued)
Bioactive molecules
or nutraceuticals Marine source Food application Main findings References
Protein hydrolysate Skipjack tuna (Katsuwonuspelamis) roe Emulsion sausage Lipid oxidation-reduction of sausages during [146]
from broadhead 12 days of storage was observed
catfish Skipjack roe protein hydrolysate did not affect
(Clarias sausages’ organoleptic properties
Nikheel Rathod et al.
macrocephalus)
Fish concentrate Sea bass (Dicentrachuslabrax) filleting Fresh pasta Nutritional value of pasta was improved; n - 3 [147]
by-products (trimmings) fatty acids remained in satisfactory quantities
during the shelf-life
Enriched pasta had acceptable sensory
properties
n - 3-rich oil Sardine (Sardinapilchardus) gill and viscera Wheat flour chips Lipid oxidation of chips was prevented and [148]
antioxidant enzymes were activated
Chips’ lipid profile was improved
Fish oil Cod liver Cooked and Fish oil was microencapsulated [149]
dry-cured Nutritional value of sausages (n - 3 content)
sausages was improved without influence on oxidative
stability, physicochemical characteristics, and
acceptability
Fish oil Cod liver Chicken nuggets Bulk fish oil and microencapsulated fish oil were [150]
added to nuggets
Microencapsulated fish oil nuggets had lower
levels of lipid and protein oxidation, and
volatile compounds
No change in sensory quality was observed for
microencapsulated fish oil nuggets when
compared to control
Fish oil Not specified Yogurt Yogurt was fortified with fish oil and nano- [151]
encapsulated fish oil
Higher n - 3 contents and better sensory
characteristics were found for yogurt fortified
with nanoencapsulated fish oil
Shrimp oil Pacificwhite shrimp (L. vannamei) Skim milk Shrimp oil was encapsulated in nanoliposomes [152]
cephalothorax β-glucan was added to mask bitterness caused by
shrimp oil
In vitro digestion showed that n - 3 fatty acids
were bioaccessible for absorption in the gut
after digestion
Oxidative stability was enhanced throughout
the storage
Shrimp oil Pacific white shrimp (L.vannamei) Biscuits Shrimp oil was encapsulated with sodium [153]
hepatopancreas caseinate, fish gelatin, and glucose syrup
before addition to biscuits
Nutritive value of biscuits was improved
No adverse effect on biscuit quality and
sensorial properties was observed after
addition of micro-encapsulated shrimp oil
Powder and sulfated Ulva intestinalis Fish fingers Lipid oxidation was retarded over 6 months of [154]
polysaccharide storage when compared to control
Products were acceptable organoleptically
Sulphated polysaccharides had better impact on
products’ texture preservation
Powder Spirulina (A. plantensis) Pasta Nutritional value of pasta was significantly [155]
improved
Pasta with spirulina had high acceptability
scores
(continued)
Extraction of Bioactive and Nutraceuticals from Marine Sources. . .
67
68
Table 2
(continued)
Bioactive molecules
or nutraceuticals Marine source Food application Main findings References
Powder Spirulina (A. plantensis) Cheese When cheese was fortified with A. platensis [156]
powder, the amount of protein and iron
increased
The positive effects on the survival of probiotic
Nikheel Rathod et al.
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Abstract
The increasing consumer awareness about the link between nutrition and health has led the food industry to
produce fortified food with bioactive compounds. Considering that not all bioactive compounds are freely
available and in the light of increasing attention to preserve environmental resources, the new trend
consisted of waste recovery of industrial food processing residues with active potential. Currently, clean
label and eco-friendly extraction methods have realized reputation accounts for the removal of solvent
usage and reduction in energy consumption. In this context, microwave-assisted extraction (MAE) evolved
as a novel procedure for the extraction of bioactives and nutraceuticals. With higher extraction efficiency,
this process was noted to consume less time and energy, and interestingly, the bioactive compound’s
functionality has not degraded. In this chapter, MAE’s potential as an eco-friendly technique was explored.
To improve its efficiency, microwave-assisted extraction has been coupled with conventional techniques.
Accessible data stress the significance of various hybrid techniques: microwave/conventional ones for the
extraction of bioactive compounds. Information about this topic could help students and scientific
researchers who are engaged in chemical engineering, chemistry, and meat technology communities to
approach the complex theme of microwave-assisted extraction.
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_4,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
79
80 Moufida Chaari et al.
Microwaves have electric and magnetic fields since they are electro-
magnetic devices. These fields lead to a heating effect via two
mechanisms, dipolar rotation and ionic conduction [19].
(i) Dipolar rotation refers to the phenomenon that occurs when
molecules with uneven distribution of charge, known as a dipole
moment, attempt to align themselves with the alternating electric
field produced by microwaves. The oscillation of these dipolar
molecules results in collisions with other molecules in the sur-
rounding medium, which then generates heat. This process hap-
pens quickly and repeatedly, making it an efficient way to convert
electromagnetic energy to thermal energy [29].
On the other hand, (ii) ionic conduction is defined as a process
that occurs when charged particles, such as ions and electrons,
move through a medium in response to an electric field produced
by microwaves. This movement or migration generates friction
between the ions and the medium, which results in the generation
of heat. The degree of heat generated by this process depends on
factors such as the strength of the electric field and the conductivity
of the medium [20].
The relative contribution of these two mechanisms to the
overall heating of the sample is largely dictated by temperature.
Specifically, as the contribution of dipole rotation decreases, the
temperature of the sample increases, while the contribution of ionic
conduction increases. It means that if a sample contains both polar
molecules and ions, then as it is heated by microwave energy, the
heating will initially be dominated by dipole rotation. The relative
contribution of these two mechanisms also depends on the mobility
and concentration of the ions within the sample [20]. Conse-
quently, these mechanisms induced the destruction of hydrogen
bonds in organic molecules, which increased solvent penetration
into the plant matrix [30] and thereby dissolution of extractable
molecules. In fact, microwave-assisted extraction (MAE) may be
summarized in two main steps as Chemat et al. [21] and Vinatoru
et al. [20] mentioned:
1. Penetration of the solvent into the plant cell by diffusion:
Initially, in the equilibrium phase, solubilization and partition-
ing phenomena come into play, which leads to the detachment
of the substrate from the particle’s outer surface at a relatively
consistent rate. This step is then followed by an intermediate
phase of transition to diffusion, where resistance to mass trans-
fer begins to appear at the interface between the solid and
liquid phases. During this period, a mass transfer occurs
through convection and diffusion.
82 Moufida Chaari et al.
Grape juice waste Water 1 g/ – 2.23 min 428 W Total monomeric anthocyanin [66]
18.43 mL yield: 1.32 mg/g
Onion peels Choline chloride: urea: 1 g/ – 15.03 min 100 W TPC: 80.45 mg GAE/g DW [67]
83
(continued)
84
Table 1
(continued)
3.2 Extraction Time Heating time is an essential factor that affects the extraction mech-
anism [19]. Furthermore, increasing time augmented extraction
efficiency and quantity of analytes [2]. However, it also increases
the possibility of the degradation of thermolabile compounds. For
the extraction of different kinds of plant matrices, various time
scales are required [38]. Sometimes, 60 s-60 min are required
for the maximum production of analytes in MAE (Table 1). Several
findings agreed that extended exposure to microwave irradiation
resulted in a greater release of phenolic compounds from Hibiscus
sabdariffa, Aegle marmelos, and Myrtus communis leaves [39–
41]. The amount of polyphenols extracted increased by over 30%
when the extraction time was changed from 5 to 29.5 min
[42]. Whereas, Belwal et al. [8] reported that 2 min was suitable
for MAE of alkaloids, berberine and palmatine with concentrations
of 46.38 mg/g DW and 20.54 mg/g DW, respectively. In the
investigation of Kadi et al. [9], it was noticed that the total
Microwave-Assisted Extraction of Bioactive and Nutraceuticals 87
3.3 Extraction The proper selection of extraction solvent is one of the key elements
Solvent and Sample- that have a significant impact on MAE’s total output. The proper-
to-Solvent Ratio ties of the solvent (nature, polarity, solubilization, purity, etc.) are
other variables that affect the process of extraction [2]. Several
forces, such as the physicochemical interactions, may be strongly
associated with the properties of the solvent [21]. Typically, when a
solvent has a high dielectric constant and dielectric loss, it tends to
have a greater ability to absorb microwave energy. Essentially, the
capacity of the solvent to absorb this energy increases as the dielec-
tric constant and dielectric loss increase, resulting in a faster heating
rate for the solvent relative to the plant material [43]. In order to
measure relative solubility, the Hildebrand solubility parameter
scale is commonly used. This parameter is the measure of the
cohesive energy between the solvent and the matrix in a solution
[20]. In fact, δ is linked to the hydrogen-bonding capacity, the
polarity, and the dispersion coefficient. As a result, there is a signifi-
cant correlation between the polarity and the Hildebrand solubility
parameter (δ) [20]. The solvent volume is also a crucial component
to take into account since it needs to be sufficient to ensure that the
entire sample is submerged in the solvent during the whole irradia-
tion process [21]. In addition, the selected solvent must be more
selective toward the target analyte than the other matrix constitu-
ents [44]. MAE can use water as a solvent for both polar and
nonpolar compounds, making it an attractive option for more
environmentally friendly extraction processes [43]. By blending
different solvents, it is possible to alter the properties of the solvent,
resulting in differing selectivity for various compounds [43]. In
fact, the use of an ethanol-water mixture as an extraction solvent
facilitated the recovery of TPC due to its high dielectric constant
and dissipation factor, which enables the effective absorption of
microwave energy. Furthermore, this solvent mixture increased
the penetration of the solvent into the sample matrix, thereby
enhancing heating efficiency. These results are in line with the
findings of Nisca et al. [4], who carried out an optimization of
extraction parameters for aqueous and hydroalcoholic extractions,
and the total polyphenolic and tannin contents were determined.
The results indicated that the optimal extraction conditions for
aqueous (30 min at 850 W) and hydroalcoholic (18 min at
650 W) extracts were different. The hydroalcoholic bark extract
exhibited a higher yield of total polyphenols (403.73 mg GAE/g
88 Moufida Chaari et al.
3.4 Matrix MAE depends on the type of plant utilized as a raw material, which
Characteristics can produce a variety of valuable compounds as well as the compo-
sition of the chosen plant tissue/cell or part of the plant that
incorporates different kinds of components. Moreover, bioactive
and nutraceutical compounds are typically bound to other com-
pounds within plant structures, such as polyphenols, which are
uncommonly found in their unbound form. Instead, they are
often covalently linked to the plant cell wall, may exist in waxes or
on the exterior surfaces of plant organs, and are linked via glyco-
sides [49]. For example, plants’ leaves contain high content of
phenols [50]. Moreover, Rahmawatii et al. [1] reported that the
yield of extraction from Pegagan (Centella Asiatica L.) leaves is
significantly impacted by the quantity of material present. Also, the
particle size of the plant matrix is an important factor [51]. Several
studies reported that the extraction yield improved when matrix
particle size decreased [51–53]. According to Poureini et al. [52],
the apigenin extraction yield was enhanced by decreasing the parti-
cle size from 0.75 to 0.10 mm. A similar trend was depicted by Patil
et al. [53]. These authors detected an optimal range of particle size
Microwave-Assisted Extraction of Bioactive and Nutraceuticals 89
3.5 Temperature Increasing temperature until a certain level increases the extraction
yield of some bioactive compounds. In fact, Zhao et al. [55] men-
tioned that the impact of extraction temperatures was examined
while holding other variables constant (30% ethanol, 30 mL/g,
30 min, 500 W). As the temperature increased (20–50 °C), there
was a significant increase in TPC value from 23.88 to 34.46 mg
GAE/g DW. Elevated temperatures have the potential to accelerate
intermolecular interactions and molecular movement, which may
lead to increased solubility of solutes in the solvent [43]. Therefore,
the TPC value depicted a marked improvement as the extraction
temperature increased from 40 to 50 °C, but subsequently
decreased as the temperature continued to rise. Kapoore et al.
[48] noticed that an increase in temperature resulted in decreased
yields of phycoerythrin, which confirmed that thermal damage can
occur over 40 °C, while carotenoids degrade at temperatures over
60 °C. The extraction of phenolic acids from green tea was found to
be more effective at a temperature of 100 °C, whereas the flavanols
and flavonols, which are sensitive to high temperatures, displayed
better extraction yield at a lower temperature of 80 °C [56]. In
addition, according to these authors, the extraction of quercetin
glycosides is more efficient at 80 °C compared to 100 °C. This
finding could be explained by the fact that quercetin glycosides
have an oxidizable catechol ring (B-ring), making them more sus-
ceptible to thermal degradation than kaempferol glycosides, which
have a mono-phenolic B-ring. Moreover, when extracted using
MAE at a temperature of 90 °C, the sulfated polysaccharides
obtained from Ulva prolifera using an acidic solvent (0.05 M
HCl) exhibited superior water- and oil-holding capacities. Con-
versely, the polysaccharides extracted at a higher temperature of
150 °C demonstrated the best foaming properties as well as the
highest antioxidant and pancreatic lipase inhibition activities [57].
90 Moufida Chaari et al.
4.1 Solvent-Free This method involves using microwaves to perform a dry distilla-
MAE (SFM) tion on a fresh matrix, without adding any water or organic solvent.
The process involves heating of the raw material with water to
release the essential oil from glands, which is then carried away by
steam produced from the matrix water. The distillate, made up of
water and essential oil, is continuously condensed using a cooling
system placed outside the microwave oven. Any excess water is
returned inside the balloon to maintain the appropriate humidity
level of the matrix [21]. This straightforward approach allows the
efficient extraction of essential oils without the use of additional
solvents. The findings of Iftikhar et al. [22] revealed that the SFM
technique, which does not require solvents and utilizes a power
setting of 480 W and a duration of 60 s, is an efficient approach for
extracting antioxidant compounds from gourd fruit. Likewise, Wei
et al. [15] mentioned that the combination of SFM and moisture
regulation was a potent approach to extract essential oil from
deciduous leaves of C. longepaniculatum. In addition, compared
to conventional hydro-distillation, Liu et al. [5] depicted that SFM
exhibited better performance in terms of various parameters such
as extraction efficiency (3.51% in 23 min vs. 3.35% in 240 min),
initial extraction rate (3.3772 vs. 0.1868), extraction rate constant
(0.3002 vs. 0.0152), extraction capacity (3.67% vs. 3.51%),
oxygenated compound content (83.93% vs. 74.81%), energy
4.2 Focused-MAE In FMAE, the sample is placed in an opened vessel and a specific
(FMAE) area is exposed to microwave radiation. This system functions at
atmospheric pressure [78], while the maximum temperature is
provided by the boiling point of the extraction solvent utilized
[79]. Hence, it can be used for the extraction of thermolabile
components. In addition, this system is composed of a condenser
that is set on the top of the vessel to avoid the loss of volatile
compounds [80]. Therefore, the microwave reactor’s configuration
influences heat production in the reaction medium [21]. In fact,
using a central composite experimental design, the extraction of
betulinic acid from Zizyphus joazeiro was optimized by employing
FMAE technology. This analysis confirms the applicability of
FMAE extraction as a speedy, environmentally friendly, and effec-
tive extraction method. As per the study, the optimal temperature
and duration of extraction are 70 °C and 15 min, respectively
[81]. By directing microwave energy to a small region of the sample
[82], FMAE attained a more efficient extraction with less energy
consumption [81].
4.3 Ionic Liquid- The merging of microwave irradiation with ionic liquids (ILs)
Based MAE (ILMAE) presents an influential approach toward achieving high effectiveness
and less harmful procedures. ILs are liquefied salts that retain their
liquid form at low temperatures, frequently under 100 °C, and they
are comprised of organic cations and organic or inorganic anions
[83]. In comparison to conventional organic solvents, ILs exhibit
numerous distinguishing characteristics, such as trivial vapor pres-
sure, elevated temperature stability, low volatility, chemical stability,
wide electrochemical stability window, and ionic conductivity
[84]. Thus, ILs are considered as outstanding microwave absor-
bers. As stated by Li et al. [85], ILMAE can enhance the extraction
efficiency of total biflavonoids in a shorter time and with a reduced
amount of solvents, compared to conventional soxhlet extraction.
In fact, according to Motlagh et al. [6], when compared to the
commonly used conventional Soxhlet method, the protein yield
obtained under optimized conditions using choline acetate ([Ch]
[Ac])-mediated water-based MAE technique (26.35%) is much
higher, indicating the superiority of this approach over the Soxhlet
extraction method (0.63%). The results indicated that [Ch]
92 Moufida Chaari et al.
4.4 Ultrasonic MAE The concurrent utilization of ultrasonic and microwave extraction
(UMAE) methods led to a notably greater quantity of bioactive compounds
in comparison to the traditional decoction extraction techniques,
highlighting the synergistic effects of these novel approaches
(Kwansang et al. 2022). As reported by Sun et al. [12], the
Microwave-Assisted Extraction of Bioactive and Nutraceuticals 93
4.6 Microwave The MHG apparatus is essentially a microwave unit that operates
Hydro-diffusion and similarly to a standard commercial model. It utilizes a combination
Gravity (MHG) of microwave radiation and the force of gravity at ambient pressure
to perform extraction from fresh plant material [98]. As described
Microwave-Assisted Extraction of Bioactive and Nutraceuticals 95
Table 2
MAE methods for bioactive compounds extraction
5 Conclusion
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102 Moufida Chaari et al.
Abstract
Extraction is an important step in the route of phytochemical processing for the discovery of bioactive
constituents from plant materials. The extraction technique plays a significant role in the yield, chemical
structure, and bioactivity of the extracts. Ultrasound-assisted extraction (UAE) has been widely applied as a
novel, green, and rapidly developing extraction method suitable for upscaling and improving the extraction
efficiency of bioactive compounds. UAE has substantial advantages such as low consumption of solvent and
energy, simplification of manipulation and work-up, high extraction yield and purity of the final product,
and fewer damages of active compounds, over the conventional Soxhlet extraction and cold maceration.
UAE can also provide the opportunity for enhanced extraction of heat-sensitive bioactive and food
components at lower processing temperatures. Ultrasound-assisted herbal extracts exhibit higher antican-
cer, antimicrobial, and antidiabetic activities than extracts prepared through conventional methods. Nowa-
days most of the industry-based extractions are carried out using UAE as full extraction can be completed in
minutes with high reproducibility. UAE of herbal, oil, protein, polysaccharide, bioactive compounds, such
as phenolics, flavonoids, and natural colors, which have importance in food, pharmaceutical, and allied
industries, is discussed here.
Key words Ultrasound-assisted extraction, Green extraction, Cavitation effect, Bioactive compounds,
Industrial application
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_5,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
103
104 Manab Jyoti Goswami et al.
Ultrasonic cleaning baths (Fig. 1a) and the more powerful probe
systems (Fig. 1b) are the two most common ultrasound equipment
used for extraction. For large volumes of fluids, ultrasound baths or
continuous or recycled-flow sonoreactors are commonly used.
While an ultrasound horn with the tip submerged in the fluid is
sufficient for small extraction volumes. Ultrasonic devices for
extraction have also been manufactured by several companies on
an industrial scale. These devices usually have a volume capacity of
30–1000 L with a power range of 500–16,000 W [14]. Usually,
laboratory ultrasonic systems are used in batch mode, whereas flow
mode is often used in operating industrial systems.
2.1 Bath Systems 1. The basic component of an ultrasonic bath consists of a tank, an
electronic generator, and a transducer. The generator supplies
electrical power to the transducer. Generally, multiple transdu-
cers are attached to the tank on sides by epoxy resin in today’s
practice. A thermostatically controlled heater can also be
provided for the bath.
Ultrasound-Assisted Extraction for Food, Pharmacy, and Biotech Industries 107
Fig. 1 Commonly used ultrasonic extraction systems (a) ultrasound bath (b) ultrasound probe. (Reproduced
from Chemat et al. [4] with permission from Elsevier)
2.2 Probe Systems 1. Probe systems comprise a generator, transducer, and horn. The
generator supplies alternating electrical frequencies, usually
20 kHz. It allows the regulation of the amplitude and also
controls the cooling of the medium. The horn may consist of
an upper horn made of titanium and a detachable horn.
Although the detachable horn can be made of different materi-
als, titanium alloy is often used.
2. The extraction operation is carried out by immersing the probe
into the vessel with raw material and extractant. The total
volume of the mixture to be sonicated governs the choice of
the detachable horn to be used. Sonochemical effects were
found to be stronger near the tip, as most of the energy
transmitted to the medium occurs near the tip. Stepped probes
are commonly used, whereas the use of spiral probes is also
seen [17].
3. Probes for industrial use can be developed with different boos-
ters to adjust the ultrasound energy transmitted to the
medium. For continuous sonication, a closed flow cell is used
and thereby a homogeneous sonication can be achieved.
108 Manab Jyoti Goswami et al.
2.3 Probes Versus 1. The extraction process in the probe is a type of direct sonica-
Baths tion, while the process involving baths is regarded as indirect
sonication.
2. The system arrangement in the probe enables amplification and
concentration of ultrasonic energy. This in turn enhances the
sonication effectiveness compared to bath systems, sometimes
up to 100 times greater.
3. In probe systems, higher energy is transmitted to the medium
giving rise to better performance. This helps to minimize the
extraction time than in bath systems. This shortening of extrac-
tion time increases the reproducibility of probe systems.
4. Sonication in a probe leads to the generation of heat and hence
this system may not be suitable for the recovery of volatile
compounds. So, bath systems are generally preferable for the
extraction of materials containing volatile compounds.
5. Cross-contamination is easier with ultrasonic probes than with
ultrasonic baths [16].
2.4 Online UAE Online UAE is a considerably faster approach for carrying out
System extraction. It comprises an open system where fresh solvent contin-
uously flows through the sample. It leads to the displacement of
mass transfer equilibria toward the solubilization of analyzing sub-
stances into the liquid media. The extract is then passed to the
continuous manifold for online analysis. The analytical procedure
involves preconcentration, derivatization, filtration, and finally
detection of the active compounds by various available techniques
(e.g., gas chromatography mass spectrum) [18].
Advantages of online UAE
1. Sample contamination, as well as losses of analytes, is minimum
in online UAE.
2. Less consumption of reagents is observed in online UAE as
compared to offline UAE.
3. Centrifugation or the filtration step is not required in online
UAE to separate the liquid phase from the solid particles.
Thereby sample preparation can be completed in a short dura-
tion of time [19].
3 Extraction Mechanism
3.1 Basic Principle Ultrasound is sound waves having frequencies greater than 20 kHz,
which is higher than the upper audible limit of human hearing.
Usually, the output source of ultrasound is a vibrating body that
causes vibration of the surrounding medium and then the transfer
of energy from the ultrasonic wave to the neighboring particles
Ultrasound-Assisted Extraction for Food, Pharmacy, and Biotech Industries 109
3.2 UAE Mechanism 1. In UAE, ultrasound frequency in the range of 20–50 kHz is
normally used. In extracting media, ultrasound can produce
vibration, cavitation, crushing, mixing, and some comprehen-
sive effect. These effects can break the cell wall and results in
successful extraction of natural product components from plant
matrices [21, 22].
2. Normally it is believed that cavitation effects, thermal effects,
and mechanical effects have a substantial influence on UAE.
The combined results of these effects lead to the destruction of
the cell wall, reduction in particle size, and enhance the reac-
tion rate through the mass transfer of the cell wall. In general,
these effects do not cause any changes in the structure and
functions of the extracts [23, 24].
Fig. 2 Scheme of ultrasound cavitation physical process. (Reproduced from Wen et al. [26] with permission
from Elsevier)
Ultrasound-Assisted Extraction for Food, Pharmacy, and Biotech Industries 111
3.4 Factors Effecting Several parameters effect the process of UAE. To obtain a high
UAE extraction efficacy, the study of these parameters is of great impor-
tance. However, it is not always necessary to consider that yield is
the only objective of the extraction process. Moreover, minimal use
of non-renewable resources along with low energy consumption
should be taken into account. The influencing factors in UAE
include the shape and size of the ultrasonic reactor device, extrac-
tion process parameters, solvent type, temperature, and matrix
particle size [26].
3.4.1 Shape and Size of When contacts a solid surface, ultrasonic waves are reflected. In the
the Ultrasonic Reactor UAE extraction using an ultrasonic bath, the shape of the reaction
Device vessel is crucial. In order to attain a minimum reflection of waves
the use of a flat bottom vessel such as a conical flask would be the
best choice. A vessel with minimal thickness should be used to
reduce attenuation. It is necessary to compute the optimal reactor
dimension and the location of the transducer-related elements to
obtain maximum energy transfer to the fluid. In the case of ultra-
sonic probes, a rapid decrease in intensity is detected both axially
and radially. Thus, it is preferred to keep a minimal space between
the ultrasonic probe and the wall of the container. The probe
should not touch the container to avoid damage to the
material [28].
3.4.2 Extraction Process Several studies reveal that high ultrasonic power induces greater
Parameters: Power and shear forces that cause major alterations in materials. However, in
Frequency the food industry optimization of this parameter is usually per-
formed. Optimization is done to achieve the best results using
minimum ultrasonic power [29]. Generally, improvement in yield
and composition of the extract in UAE can be achieved by increas-
ing the ultrasound power.
Ultrasound frequency may also influence the extraction process
and have to be optimized. The optimal choice of ultrasound fre-
quency enables to obtain the desired cavitation effect. An increase
in the ultrasound frequency or intensity in the extraction process
leads to the gradual decrease of the liquid cavitation bubbles. The
high frequency suppresses the compression-rarefaction cycles,
which is more difficult to induce acoustic cavitation bubbles due
to the short period. While the low frequency may reduce the
formation of transient cavitation bubbles [30]. The effect of fre-
quency not only influences the cavitation bubble size but is also
related to the mass transfer in the extraction process. Ultrasound
frequencies in the range of 20–100 kHz are commonly used in
UAE. Thus, optimization of the frequency is important for ultra-
sound extraction [4].
112 Manab Jyoti Goswami et al.
3.4.3 Solvent Selection of the most appropriate solvent for extracting the analytes
from the sample matrix is an important step of UAE. Ultrasound
extraction is largely influenced by the amount and type of solvent
used, concentration, and the ratio of solvent and solute. These
factors contribute to the transmission of ultrasonic energy. The
initiation of cavitation is affected by the physical properties of the
solvent such as viscosity, surface tension, and vapor pressure
[31]. The collapse of the cavitation bubble is more intense in
solvents with low vapor pressure compared to that of the solvents
with high vapor pressure. So, a solvent with low vapor pressure is
generally preferred in UAE [4].
3.4.4 Temperature and Sonochemical effects are favored by low temperatures as the cavita-
Time tion effect is prominent at lower extraction temperatures. Although
high temperature enhances solvent diffusion rates, it could lead to
the degradation of thermolabile compounds. At higher tempera-
tures, the collapse of cavitation bubbles may be reduced and conse-
quently, sonochemical effects are less effective. Therefore, the
temperature of the solvent should be controlled within a suitable
range to obtain the highest yield of the target compounds. Simi-
larly, the extraction time should be optimized. Short time may
result in incomplete extraction and very long extraction time may
induce undesirable reactions and less selective extractions [32].
3.4.5 Particle Size of the UAE yield may also be effected by the size of the matrix particles.
Matrix Usually, the reduction of particle size increases the surface contact
area. When particles of the matrix are small enough, most cell walls
are disrupted by ultrasound, thus facilitating better extraction [32].
4.1 UAE of Fruits, Fruits and vegetables are the sources of a wide range of secondary
Vegetables, and Their metabolites present in their pulp, seed, peel, and bark. Various
By-Products phytochemicals, antioxidants, lipids, pigments, aromas, and other
molecules of industrial importance have been extracted from fruits
and vegetables. Laboratory-based extraction of these molecules can
be integrated further for their applications in the food, pharmaceu-
ticals, biotech, and cosmetics industries. Extensive use of UAE for
the extraction of such bioactive components has been observed.
UAE has substantial advantages for extracting such compounds
from fruit and vegetable matrices over conventional extraction
techniques. Using UAE, bioactive component extraction can be
performed in very short time, at a relatively low temperature, with
optimal energy and solvent requirement. As a non-thermal extrac-
tion technique, UAE facilitates the retention of the functionality of
bioactive compounds [33].
Ultrasound-Assisted Extraction for Food, Pharmacy, and Biotech Industries 113
Table 1
Enhancing effect of UAE on antioxidant capacity compared to conventional extraction methods
4.1.3 Extraction of UAE is a promising tool for the extraction of phenolic compounds
Polyphenols for laboratory and industrial purposes. Phenolic compounds are
widely used in wine industries for providing characteristic color
and flavor in wine samples. Most of the plant-derived polyphenolic
compounds exhibit antioxidant properties and can serve as natural
116 Manab Jyoti Goswami et al.
Table 2
UAE of pectin from different fruit and vegetable by-products
4.1.5 UAE of Anthocyanins and carotenoids are the natural color pigments pres-
Anthocyanins and ent mostly in fruits and vegetables. In present times, natural colors
Carotenoids are very demanding in the food industry. Increasing use of antho-
cyanins as natural colorants mostly in food products and beverages
has been observed. Anthocyanins are also used as bioactive com-
pounds in pharmaceutical industries which further boosted their
market requirements. Similarly, carotenoids have been used as bio-
active compounds in pharmaceutical and allied industries.
118 Manab Jyoti Goswami et al.
Table 3
UAE of bioactive flavonoids
Extraction parameters
4.1.6 Extraction of Edible UAE has been recognized as a valuable extraction method in the
Oils edible oil industries to improve yield and reduce the duration of
extraction time. Rapid extraction of oil from soybeans using high
frequency ultrasound waves was reported in the literature. The
yield was significantly improved in UAE [90]. Garcia and Castro
reported that ultrasound-assisted Soxhlet extraction is an effective
method for the extraction of a higher amount of oil from raw
matrices. They used this combined methodology and extracted a
higher amount of total fat content from soybean, sunflower, and
rape seeds than the Soxhlet extraction performed alone [91]. The
benefit of ultrasonic pre-treatment of oleaginous seeds before oil
extraction was also reported. Ultrasonic pre-treatment of the
almond and apricot seeds prior to oil extraction provided better
yield with a reduction in extraction time [92]. Application of UAE
on the extraction of oils from different food by-products, such as
rice bran, soybean germ, and papaya seed, has also been reported.
4.2.1 Extracts with Anticancer activities of herbal extracts are mainly associated with
Anticancer Properties the polyphenolic compounds they possess. Polyphenols have the
ability to prevent cancer by diminishing or hindering the harmful
effects of free radicals on cells through their scavenging properties.
Their diverse chemical structures allow them in neutralizing free
radicals produced in the body. Polyphenolic compounds can pre-
vent oxidative stress to a level that does not harm cellular DNA and
regulatory protein synthesis metabolism. The importance of UAE
in cancer studies is mainly due to its capability in preserving the
anticarcinogenic properties of polyphenols in plant extracts. Activ-
ities of ultrasound extracted polyphenols have been studied exten-
sively in both in vitro and in vivo systems [95]. Polyphenols
extracted with ultrasound assistance from Thelephora ganbajun
exhibited superior antiproliferative activities toward human breast
(MCF-7), liver (HepG2), lung (A549), and colon (HT-29) cancer
cells compared to Soxhlet and maceration extraction methods
[96]. Polyphenolic compounds extracted from Trapa quadrispi-
nosa Roxb. showed effective antitumor action against Hela,
HepG2, and U251 tumor cells [97]. Berkani et al. used UAE to
prepare the extract of the herbal plant Zizyphus lotus. The extract
was found to contain a high amount of total phenolic and flavonoid
contents. The herbal extract significantly inhibited cell proliferation
on the MCF-7 and HepG2 tumor cell lines with IC50 values of
<0.05 and 3 ± 0.55 mg/mL, respectively [98]. Extracts of Oci-
mum basilicum and Ocimum canum were found to reduce the
proliferation of human breast cancer cells MCF-7, when extracts
were prepared ultrasonically as reported by Koolamchal et al.
[99]. Thus, UAE can preserve and enhance the anticarcinogenic
and antitumor activities of polyphenol extracts.
4.2.3 Extracts with Reports suggest that UAE improves the antidiabetic properties of
Antidiabetic Properties herbal extracts. Sunita et al. investigated the in vivo antidiabetic
properties of Gymnema sylvestre leave extracts prepared through
UAE and Soxhlet extraction. It was found that insulin released
from rat pancreatic RINm-5 F β cells was affected by the extracts
prepared by both the methods and the amount of extract used. The
ultrasound-assisted extract at a concentration of 100 μg/mL
showed up to about four times more insulin production from
RINm-5 F β cells than extracts obtained from Soxhlet extraction
[106]. Hypoglycaemic properties of ultrasonically extracted aque-
ous crude extracts of Azadirachta indica, Bryophyllum pinnatum,
Carica papaya, and Mikania cordata were measured by Sadat et al.
They have carried out in vivo studies on artificially developed
diabetic mice. According to their report, A. indica, B. pinnatum,
and C. papaya significantly reduced the plasma glucose level below
126 mg/dL. The effect was observed almost similar to the standard
antidiabetic drug glibenclamide, which reduced the plasma glucose
level to 100.35 ± 12.32 mg/dL [107].
These observations accomplished that UAE significantly
enhances the anticancer, anti-inflammatory, and antidiabetic prop-
erties of herbal extracts. This explains the importance of the phar-
maceutical application perspectives of the UAE.
122 Manab Jyoti Goswami et al.
5.1 Combination of For fast and efficient extraction, the Combination of UAE with
UAE with Microwave Assisted Extraction utilizing simultaneous irradiation is
Microwave Assisted one of the most promising hybrid techniques. It is commonly used
Extraction for the extraction of oils from vegetable sources (Fig. 3a).
Fig. 3 Hybrid extraction techniques (a) ultrasound-microwave extraction, (b) ultrasound-supercritical fluid
extraction, and (c) ultrasound-DIC extraction. (Reproduced from Chemat et al. [4] with permission from
Elsevier)
Ultrasound-Assisted Extraction for Food, Pharmacy, and Biotech Industries 123
5.3 Combination of Applications of this hybrid technique have been seen in vegetable
Ultrasound and oil industries and the production of sugar, wine, and fruit juices.
Extrusion Extraction
5.4 Combination of Application of this combined technology was seen in the sequential
UAE and Instantaneous extraction of oil and antioxidants. Using this hybrid technology, it
Controlled Pressure was possible to improve the kinetics and yields of antioxidant
Drop Process (DIC) extraction [108] (Fig. 3c).
6 Conclusion
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Ultrasound-Assisted Extraction for Food, Pharmacy, and Biotech Industries 127
Abstract
Alternative methods are currently being investigated to reduce the overuse of organic solvents, which have
serious environmental and health consequences. Certain promising green technology-based alternative
extractions are employed in a wide range of bioactive and nutraceutical extractions, including ultrasonica-
tion, microwave-assisted extraction, pressurized liquid extraction, and enzyme-assisted extraction. Super-
and subcritical fluid extractions, on the other hand, are sufficiently sophisticated green technologies that
have superior efficacy and selectivity for the extraction of nonpolar and low-polar constituents. In this
regard, this chapter gives an overview of the process, the theory of super- and subcritical extraction, and the
role of pivotal variables for optimal extraction. Additionally, recent findings of the principal phytochemical
and bioactive compounds extracted by this process with their nature, biological activities, and stability
during and after processing are discussed.
Key words Supercritical fluid extraction, Subcritical fluid extraction, Natural products, Pharmaceuti-
cal, By-products
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_6,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
129
130 Pankaj Koirala et al.
4.1 Sample and In both subcritical and supercritical fluid extraction, a sample with a
Its Preparation smaller particle size has an increased interfacial area and minimal
diffusion paths of raw material, which improves the solute extrac-
4.1.1 Sample Matrix
tion rate. An investigation by Peng et al. [8] on the extraction of
and Size
tocopherol from roselle seed oil by SC-CO2 extraction under the
given conditions (temperature: 40 °C and pressure: 30 MPa)
demonstrated that the yield was lowered with increasing particle
134 Pankaj Koirala et al.
size. The size of the solid matrix governs the mass transfer kinetics,
as small molecules diffuse easily and access the supercritical fluid
throughout the sample matrix. However, extraction from the small
sample matrix has the drawbacks of compound re-absorption and
clumping, which can decrease fluidized bed velocity, clog the filters,
and eventually decrease extraction efficiency. Thus, the optimal
particle size of the sample is recommended to maximize extraction
yield while minimizing the possibility of particle agglomeration
[3, 9].
4.1.2 Moisture and The extraction rate and yield are significantly influenced by the
Equilibrium Time moisture content of the sample. The extraction yield is generally
unaffected by a small amount of moisture, but yield steadily
decreases as the moisture percentage increases in the sample.
Kostrzewa et al. [10] investigated the effect of moisture content
on extraction yield and found that moisture had no effect on
carotenoid extraction and extraction efficiency until the moisture
content was less than 7.5 g/100 g. However, the higher moisture
in the sample showed lower carotenoid recovery and also necessi-
tated carotenoid concentration after separation.
4.4 Extraction The crossover behavior of the supercritical fluid in the solubility
Parameters isotherms is observed by the pressure-temperature relationship and
its effect on density and volatility. On increasing the temperature,
4.4.1 Temperature
the density decreases under the isobaric process, while the volatility
of the solute increases with temperature, thus reducing the extrac-
tion rate. Inversion pressure (crossover pressure) has the critical
role in defining temperature selection for optimum extraction. To
clarify, low temperature permits density to dominate under the
crossover pressure that leads higher extraction yield, while over
crossover pressure, higher temperature allows solute vapor pressure
to dominate, resulting higher extraction [3].
At the subcritical phase, increasing temperature improves the
dissociation constant by decreasing surface tension, where mass
transfer is supported by the disruption of intermolecular forces in
the sample matrix and increased solubility. The diffusivity of sub-
critical water, for example, increases with increasing temperature,
whereas the dielectric constant, surface tension, and viscosity are
significantly reduced. Low dielectric constants facilitate the extrac-
tion of low-polar organic compounds due to high solubility in
low-polarity fluids [18]. On the adjustment of pressure-
temperature, one should be conscious of the maximum tempera-
ture for the extraction of selected compounds because high tem-
peratures change the structural composition by causing thermal
degradation reactions and the neoformation of Maillard com-
pounds [13, 19].
4.4.2 Pressure Under the constant temperature, the solubility of the bioactive
compounds increases with increasing pressure due to an increment
in density and solvation power, which successively increases the
extraction kinetics. However, extremely high pressure hinders
fluid diffusion [20], which could reduce yield. Thus, optimal pres-
sure based on extract specificity is preferred. The effect of the
pressure, which is also dependent on temperature variation,
depends on the types of selected compounds. If the pressure is
near the critical pressure, solubility increases with decreasing tem-
perature, whereas at higher pressures, solubility increases with
increasing temperature.
136 Pankaj Koirala et al.
4.4.3 Flow Rate The flow rate of the sub- and supercritical solvents has a direct
impact on the solvent-to-feed ratio, contact time, and mass transfer
resistance. Increasing the flow rate improves extraction efficiency by
minimizing the mass transfer resistance. With the low flow rate, the
solute saturates in the solvent as the result of axial dispersion, while
for the very high flow rate, yield is minimal due to insufficient
contact time [21], indicating the appropriate flow rate as a crucial
factor for maximum yield. However, too high solvent flow rate
cause substantial dilution of the extracts, necessitating an additional
concentration step following extraction [1].
4.4.4 Time Initially, the extraction yield in super- and subcritical fluid extrac-
tion increases with time, but with prolonged extraction time, this
rate drops. An investigation of the tocopherol yield from roselle
seed oil by supercritical fluid extraction demonstrated an increment
in extraction yield with increasing temperature for a certain time,
which was limited afterward [8]. This can be explained by the fact
that the process reached the saturation point and/or by thermal
degradation of bioactive compounds [22]. Consequentially, the
yield tends to decline with increasing extraction time. In contrast,
too short extraction time results in minimal solid-solvent interac-
tion, leading to a low yield.
solvent into the feed matrix affecting the yield. Investigation for
cost cutting on the extraction technique has unfolded possibilities
on other method than SC-CO2 extraction. Comparative study
against SC-CO2 extraction has presented evidence on subcritical
alcohol extraction being less time intensive, lower cost to operate,
and more convenience on separating solvent from solute.
It has shown promising application on the valorization process
too. Agro-based by-products have massive potential as a bioactive
compound source, so they are going under an extensive up cycle
assay. Apart from that, industrial waste, such as herbal medicine
wastes (HMWs) are also eligible for valorization into high value
bioactive compounds [55]. By-products, such as spent coffee
grounds, were investigated for the extraction of phenolic com-
pounds by using SWE technique [56]. The extraction time was
crucial during the extraction process because the longer extraction
time yielded less phenols from the spent coffee grounds. Similar
drop in phenolic compound (ƞ-caffeoyl-quinic acid) was observed
when extraction time was extended. The extended time favors the
oxidation of phenolic compound and extensive extraction temper-
ature also aids oxidation process [57]. The innate requirement of
extended time and high temperature for SWE shown detrimental
effect on the bioactivity of the extracts, hence to minimize the loss-
SWE could be combined with the pretreatment (microwave, ultra-
sonication) of the raw material [58].
The combined application of SC-CO2 and sequential subcriti-
cal hydrothermal liquefaction (SC-HTL), Mathur et al. [59]
extracted high value products such as, PUFAs (eicosapentaenoic
acid, docosahexaenoic acid, etc.), aromatics, aldehydes, and alkynes
from the microalgal biomass. During the valorization of biomass
(Chlorella sp. and Phormidium sp.), the utilization of all the frac-
tion was achieved, and additionally, compared to conventional
(Soxhlet) extraction method—the quality was higher. Green extrac-
tion technologies are also enabling the exploration of other plant
biomass as a source of bioactive compound. Foliage—otherwise
waste of different plants are being assayed as a potential source of
bioactive compound [60]. Some of the example are as follows:
Goyeneche et al. [61] recovered total phenols from leaves of beet-
root (Beta vulgaris L.) by using SC-CO2 extraction technique.
Similarly, Essien et al. [62] used subcritical water extraction tech-
nique to recover phenolic compounds from Kānuka (Kunzea eri-
coides) leaves. The extraction efficiency was directly proportional to
the adjustment of the extraction parameters, especially, extraction
time, temperature, and solid-solvent ratio. Assessment displayed
that there is untapped possibilities for the cheap source of bioactive
compound which could be exploited via optimized green extrac-
tion technologies.
Super- and Subcritical Fluid Extraction of Nutraceuticals. . . 143
Fig. 1 A general overview of the characterization of extracted bioactive compounds. (Source: Azmir et al. [65])
144 Pankaj Koirala et al.
8.1 Extracts The most common assessment techniques for in vitro characteriza-
Bioactivity tion are antioxidant activity using DPPH, FRAP, and ABTS [71],
antidiabetic activity using an α-amylase inhibitory assay, anti-
8.1.1 In Vitro
inflammatory activity using the protein denaturation inhibition
Characterization
technique [72] and anticancer activity using cell viability determin-
ing 50% inhibition concentration (IC50) [73]. The most efficient
SC-CO2 extract had maximum cannabidiol (CBD) and was rich in
α-pinene, β-pinene, β-myrcene, and limonene. Under concentra-
tions from 10.42 to 66.03 μg/mL, extract doses exhibited inhibi-
tory effects against E. coli, P. aeruginosa, B. subtilis, and S. aureus
[74]. In addition, the observations of antioxidant activity show that
the percentage of antioxidant activity decreased in the order of
α-tocopherol > SCO2-extracted oil > solvent-extracted oil >
Super- and Subcritical Fluid Extraction of Nutraceuticals. . . 145
8.1.2 In Vivo Analysis For the newly identified bioactive molecules, to support this typical
(Clinical Trial/Animal Study) statement, clinical trials are required to show a bioactive com-
pound’s efficacy. Clinical trials designed to ascertain the pharmaco-
kinetics, bioavailability, efficacy, safety, and drug interactions of
newly created bioactive compounds and their formulations must
be considered (extracts). Before the treatment is widely adminis-
tered to patients, clinical trials are meticulously planned to safe-
guard the participants’ health as well as provide findings to
particular research questions by evaluating their results and check-
ing for both short- and long-term negative effects [76]. Raspberry
oil extracted by supercritical CO2 has potent anticarcinogenic prop-
erties via suppression potential against several carcinoma cell lines
(colon adenocarcinoma, doxorubicin-resistant colon adenocarci-
noma, breast cancer, doxorubicin-resistant breast cancer, and lung
cancer cell lines). Raspberry oil extraction using supercritical CO2
significantly increased free radical production and DNA strand
damage in cancer cells, particularly doxorubicin-resistant lines,
implying effective targets on cancer cell vulnerabilities [77]. Extrac-
tion of the bioactive under optimized SC-CO2 extraction has
potentially higher in vivo bioactivity. Animal studies have revealed
that compounds such as curcuminoids, oleoresins, and total vola-
tiles have potent bioactive functions [78].
146 Pankaj Koirala et al.
8.1.3 Toxicity Assay Several toxicity assays are conducted to determine its safety before
clinical trials. Cytotoxicity test of the bioactive compounds are
generally carried out on VERO and MDCK cells using a MTT
assay. A decrease in the cells viability indicates the toxic effect of
that test compound. Acute oral toxicity is determined from LD50
technique. Other toxicity tests, such as body weight change (drastic
gain/loose), hematological and biochemical analysis, and in silico
prediction of toxicity, are carried out to evaluate short- and long-
term toxicological profiles [79].
It has been discovered that SC-CO2 is selective in the extrac-
tion of desirable chemicals, leaving no harmful residues in the
extracts and posing no threat to the processed product’s thermal
stability. Actually, the use of SC-CO2 extracts in food products is
frequently acknowledged as safe. With potential applications for the
extraction of important chemicals from solid plant matrices and
seed oil, SC-CO2 extraction has grown quite mature. While other
fluids, such as propane, can be used to extract plant material, CO2
offers more advantages due to its nontoxicity and favorable ther-
modynamic properties, which make it easier to employ under
supercritical conditions (over 31.1 °C and 7.4 MPa) [80]. Peterson
et al. [81] looked at how high temperatures affected the oil during
subcritical oil extraction. Peroxide readings were discovered to be
less than 5 ppm, which indicates no oxidation when compared to
Soxhlet. The FFA results also indicated that using the subcritical
approach did not result in any appreciable oxidation deterioration.
Only little amounts of ethanol (30 mg/day authorized daily expo-
sure) can be utilized for food extractions because it is a class
3 solvent and Petroleum ether is considered as class 4 because of
its less toxicity as compared to class 1 and 2 solvents [82]. Con-
trarily, water has no such health-based exposure restriction.
8.2 Stability of Bioactive compounds are mostly heat-liable. Heat treatment has a
Bioactive Compounds significantly destructive effect on polyphenols, similarly, other fac-
tors such as oxygen, light, and pH tend to accelerate the degrada-
tion of bioactive compounds causing a loss in their therapeutic
functions. Also, due to the acidic environment in our gastrointesti-
nal tract, that is, in the stomach, most of the bioactive compounds
lose their bioactivity [83]. So, for increasing the stability and bio-
availability different new techniques are used. Some of them cur-
rently used in food and pharmaceutical applications are protecting
bioactive compounds from severe exposure to external environ-
ments by storing them in moisture, air and light barrier containers,
storage at low temperatures, etc. [84]. Furthermore, encapsulation
(microencapsulation, nanoencapsulation) and emulsification are
the most widely used methods. The most modern techniques
involve microencapsulating bioactive and using nonthermal
Super- and Subcritical Fluid Extraction of Nutraceuticals. . . 147
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Supercrit Fluids 145:10–18
Chapter 7
Abstract
Solvent extraction techniques have a wide range of uses in analytical chemistry, including large-scale
industrial separations, waste management, the pharmaceutical and biochemical industries, and both inor-
ganic and organic chemistry. For the extraction of nutraceuticals from plants, a number of novel techniques
have been developed, including accelerated solvent extraction, supercritical fluid extraction, ultrasound-
assisted extraction, and microwave-assisted extraction. These techniques aim to reduce extraction time,
increase extraction yield, and improve the quality of extracts while also consuming less solvent. Solvent
extraction methods are currently frequently used in separation technologies. Recovery, concentration, and
separation of organic acids and acid mixtures are of great interest to researchers. Both the conventional and
traditional precipitation techniques and various more recent efforts to develop extraction-based process
technologies. The main problem with current solvent extraction separation is that the majority of methods
are empirical, distinctive, and exclusive to particular application domains, requiring a lot of testing. This
review offers a succinct look at the most recent developments in new solvent extraction separation
techniques for the application of bioactive extraction in the food and nutraceutical industries.
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_7,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
153
154 Ratnnadeep C. Sawant et al.
2 Water as a Solvent
are collected. The system can also be fitted with a coolant mecha-
nism to allow for the quick cooling of the extracted product.
Despite the fact that this method has often been applied as a
batch process, research of continuous methods and the online
coupling of a subcritical water extraction (SWE) system to an
HPLC apparatus via a solid phase trapping have been reported [7].
3 Organic Solvents
Table 1
Common organic solvents present in the list of hazardous air pollutants published in 2002 by the
US EPA
Table 2
Critical properties of several solvents used in supercritical fluid extraction (SFE)
Critical Property
Solubility parameter
Solvent Temperature (°C) Pressure (atm) Density (g/mL) δSFC (cal-1/2 cm-3/2)
Ethene 10.1 50.5 0.200 5.8
Water 101.1 217.6 0.322 13.5
Methanol -34.4 79.9 0.272 8.9
Carbon dioxide 31.2 72.9 0.470 7.5
Ethane 32.4 48.2 0.200 5.8
Nitrous oxide 36.7 71.7 0.460 7.5
Sulphur hexafluoride 45.8 37.7 0.730 5.5
n-Butane -139.9 36.0 0.221 5.2
n-Pentane -76.5 33.3 0.237 5.1
4.1 Aqueous Two- The first of these employs two-phase separation systems, which
Phase Systems as combine aqueous solutions with polymers and inorganic salts to
Extractants form two phases that are primarily composed of water. Using
supercritical circumstances, a second system converts the initial
two-phase system into a single phase under unique temperature-
pressure conditions. Additionally, by encapsulating the active
organic compound inside the aqueous center of a micelle of
surface-active chemicals, the active organic compound can be pro-
tected from the organic diluent. As is explained below, all of these
systems are currently the subject of active research.
Organic salts with a melting point less than 100 °C are ionic liquids
(ILs). If the salt is liquid at room temperature, they are referred to
as room-temperature ILs. They typically consist of an organic or
inorganic anion and a bulky, poorly coordinating organic cation.
When air- and water-stable ILs were first synthesized in the early
1990s, chemists were interested in ILs [17]. ILs have a wide range
of uses in chemistry and are sometimes referred to as a “green
alternative.” They are frequently combustible and explosive and
have low vapor pressures, which suggests they have less of an impact
on the environment than VOCs. ILs are helpful in liquid–liquid
extraction (LLE), liquid phase microextraction (LPME), and solid
phase microextraction (SPME) due to their low vapor pressure and
strong solubility for both inorganic and organic chemicals
[18]. Studies of the deep eutectic solvent (DES) extraction mecha-
nism, particularly extraction by the creation of a deep eutectic
system (DESys), have found similarities between the DES- and
ionic liquids (IL)-based extraction systems. Xiao et al. presented
new uses for ILs and DES in the extraction of nutritious natural
compounds [19]. In the mechanochemical extraction of target
chemicals from Moringa oleifera leaves, the extraction behavior of
choline chloride (ChCl) and 1-(2-hydroxyethyl)-3-methylimidazo-
lium chloride ([HMIm][Cl]) in DES and IL, respectively, was
thoroughly investigated.
5.1 Properties of ILs ILs have a variety of fascinating and distinctive characteristics, one
of which is extremely low vapor pressure. ILs fundamentally do not
evaporate under typical process operating conditions. The use of
ILs as industrial solvents to replace VOCs and so remove a source of
air pollution as well as risks from inhalation and explosion has thus
attracted a lot of interest [20]. Additionally, ILs maintain their
liquid state throughout a huge temperature range (e.g., 70–400 °
C). Both of these characteristics, a negligible vapor pressure and a
Novel Solvent Based Extraction 163
wide liquidus range, will make it easier to recover and repurpose ILs
in the context of LLE and hence bring financial advantages (such as
a make-up required and solvent loss that are incredibly low). Some
ILs can remove hydrophobic substances due to their hydrophobic
nature [21]. However, using the proper chelators or ligands that
could form complexes to improve the hydrophobicity of the metal
species, cationic compounds can be successfully recovered from
hydrophobic ILs [22]. The following factors are those that deter-
mine how well metal ions are extracted: (1) The side chain length
and IL structure, which alter the hydrophobicity and increase
partition coefficients [23]. (2) Selectivity should be maximized by
the ligand utilized. (3) The system’s pH [24].
5.2 Toxicology The possibilities provided by ILs, with their several million possible
Considerations structures created by combining various cations and anions, also
pose an uncommon issue in terms of defining or identifying the
toxicity and adverse impacts of those compounds on the environ-
ment. ILs are novel compounds that have not yet gained wide-
spread acceptance. It is challenging for traditional scientists to
abandon theories that have sprung out from the fertile ground of
molecular solvents over millennia. The number of laboratories that
work with ILs has increased significantly in recent years, particularly
in China. Of course, it’s crucial to have a complete awareness of the
potential health risks and environmental effects of ILs.
Unfortunately, research has shown that the initial generation of
ILs, which were based on imidazolium or pyridinium cations, were
oftentimes much more harmful than conventional solvents. The
goal for the elimination of the most harmful IL structures is the
development of simple toxicity tests to enable quick and affordable
identification of the best IL structures. Selecting only the most
suitable candidates for application, the remaining candidate struc-
tures can be examined using minimum inhibitory concentrations
(MICs) and minimum biocidal concentrations (MBCs) tests,
growth rate measurements, and EC50 (medium effective concen-
tration) calculations.
Imidazolium, pyridinium, phosphonium, and ammonium
cations were not found to have low freshwater toxicity with EC50
values below 100 mg/L, according to certain researches [25]. No
matter the kind of cation, the length of the substituted alkyl chain
on the cation had a substantial impact on the toxicity; for example,
ILs with eight carbon atoms (C8) were shown to be more toxic
than those with six and four. Due to their extensive structural
variety, ILs appear to have a particularly promising future in sepa-
ration approaches. Technologists need thorough research to hasten
the introduction of new nontoxic ILs in the created new separation
processes because certain ILs are harmful and cannot be considered
as general green replacement solvents.
164 Ratnnadeep C. Sawant et al.
Table 3
Solubilities of bio-derived solvents in water
8.1 Carboxylic Acids For the purpose of separating organic and amino acids from fer-
Separation mentation broth, solvent extraction has been suggested as an alter-
native [31]. High molecular weight amines and organophosphate
solvating agents can both be used to extract citric acid. Important
requirements have been defined for the solvent extraction process
used to produce citric acid: A distribution coefficient of 10 or below
enables simple water stripping. Although the citric acid may be
recovered using a base, the production of a citrate salt would
require additional processing as in the typical flow sheet, eliminat-
ing the benefits of solvent extraction. This is why stripping with
water is crucial.
8.2 Amino Acids Because amino acids include both carboxyl (-COOH) and amino
(-NH2) groups, they exhibit cation-like behavior at low pH,
anionic behavior at high pH, and zwitterion behavior at intermedi-
ate pH levels. Their solubility in nonpolar diluents is limited despite
the fact that they have no net charge in this intermediate pH range
due to their hydrophilicity. Additionally, its extraction using oxygen
donor extractants with carbon bonds is subpar. In order to extract
an amino acid, it is typically necessary to change it into one of its
ionic forms and then utilize an appropriate ion-pair extractant.
Because the amino acid has a net negative charge in high pH
Novel Solvent Based Extraction 167
8.3 Citric Acid For the purpose of separating organic and amino acids from fer-
mentation broth, solvent extraction has been suggested as an alter-
native [33]. High molecular weight amines and organophosphate
solvating agents can both be used to extract citric acid. Important
requirements have been specified for the solvent extraction proces-
sing of citric acid: A distribution coefficient of 10 allows for simple
water stripping. Although the citric acid may be recovered using a
base, the production of a citrate salt would require additional
processing as in the typical flow sheet, eliminating the benefits of
solvent extraction. This is why stripping with water is crucial.
Temperature had an impact on a diluent’s extraction, which
decreased as temperature rose. So, an effective technique was devel-
oped by extraction from the broth at room temperature and water
stripping at a higher temperature (60–70 °C). The creation of
emulsions and the resulting poor separation made it difficult to
extract using long-chain amines.
8.4 Extraction of Oil A difficult task in calculating the total economics of fuel production
from Algae Biomass is the extraction of fuels from microalgae biomass. It has been
discovered that the commonly used extraction techniques call for
either more sophisticated machinery or challenging processing
conditions. The goal of the innovative extraction technique is to
remove the oil from the biomass using a combination of solvent
extraction and magnetic stirred agitation. When compared to
extraction techniques such as supercritical extraction and nano-
assisted extraction, which are actively being researched, this tech-
nology has been shown to be more cost-effective. If magnetic
stirred or electromagnetic-assisted agitation is used on a commer-
cial scale, the use of magnetic stirrer-based extraction for sustain-
able biofuel production may lead to new dimensions [34]. This
method uses natural algae biomass for oil extraction.
8.5 Bioactive from In a variety of culinary products, compounds from marine algae
Marine Algae have been employed as gelling, thickening, and emulsifying agents.
Apart from being a rich source of iodine historically, sea algae were
not recognized as a source of health-promoting chemicals in the
West [35]. Marine algae are a rich source of nutraceuticals with a
variety of biological activities, according to a recent study on func-
tional food ingredients [36]. Dietary fiber, sulfated polysaccharides,
omega-3 fatty acids, amino acids, bioactive peptides, vitamins,
minerals, and carotenoids are all abundant in marine algae. These
168 Ratnnadeep C. Sawant et al.
9 Pharmaceutical Separations
9.1 Production of Before being given to the first extraction step, where it is in touch
Penicillin with substances like butyl acetate, the fermentation broth contain-
ing penicillin is first filtered to remove mycelium and pH-adjusted
to 2–2.5 to convert it to the mostly undissociated penicillanic acid
[40]. The partition coefficient and penicillin stability have been
compromised to determine the exact pH that is employed. How-
ever, if it becomes necessary to create pure penicillin for pharma-
ceutical use, it can be refined by reextraction at pH 2–2.5 and
further stripping with a phosphate solution at pH 6. The majority
of penicillin is utilized as intermediates in the synthesis of, for
example, cephalosporin. This penicillin extraction is an illustration
of the direct partitioning of a solute using a polar organic molecule.
Utilizing organic chemicals that form ion pairs with penicillin is a
different method that has been taken into consideration. Here, the
authors discovered that in the pH range 5–7, where the product is
most stable, the penicillin anion could be extracted effectively with
a secondary amine (Amberlite LA-2). This method, which is widely
employed in hydrometallurgy, can be utilized to extract either
cationic species using organic acid anions or anionic species utiliz-
ing cations, as was previously demonstrated. While a hydrocarbon
diluent is typically used in hydrometallurgy, more polar diluents are
typically needed for medicinal applications. Ion pair creation is used
in a number of other biotechnology systems, even though the
adoption of such chemically assisted extraction procedures is
unlikely to replace the current extraction processes for the commer-
cial extraction of penicillin.
Novel Solvent Based Extraction 169
11 Concluding Remarks
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Chapter 8
Enzyme-Assisted Extraction
Sadhana B. Maled, Ajay R. Bhat, Subrahmanya Hegde, Yuvaraj Sivamani,
Arunachalam Muthuraman, and Sumitha Elayaperumal
Abstract
The extraction of compounds from plant and animal sources that have medicinal properties are known as
bioactive compounds, which can either improve health or can be hazardous. As novel natural compounds
from various plants are uncovered, we are discovering more biologically active compounds. Enzymes can be
employed to extract such bioactive compounds by rupturing plant cells. The extraction of a bioactive
compound such as stevioside from a stevia plant with the assistance of enzymes is a better example of
processing with potential utility for the food sector. The extraction of bioactive compounds from plant
sources with the help of environment-friendly enzymes, especially for food, nutraceutical, or pharmaceuti-
cal uses, is a cutting-edge technology used in these industries. This study explains the overall idea about
bioactive compounds, their extraction processes, importance, and uses.
Key words Bioactive, Stevioside, Stevia, Enzymes, Enzyme-assisted extraction, Nutraceutical, Bio-
technological applications
1 Introduction
The chemical compounds that are produced in the plant, which are
not involved in the metabolic activity of the plant, are mostly
secondary metabolites. These are biologically active compounds
[1]. These are produced by the subsidiary pathways. These bioac-
tive compounds have antioxidant, anti-inflammatory, and antimi-
crobial properties and greater immunomodulatory potential
properties. Detailed information about secondary metabolites and
their application is mentioned in Table 1. These compounds pos-
sess additional nutritional value to the food that is generally found
in less amount, which provides health-related benefits over the
product’s basic nutritional value [2]. These compounds include
pharmaceuticals, flavors, fragrances, cosmetics, food additives,
feedstocks, and antimicrobials. These compounds are produced
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_8,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
173
174 Sadhana B. Maled et al.
Table 1
Type of chemical class, plant source, and enzyme used for the extraction of specific bioactive
compounds
2.1 Extraction The process of extraction involves the separation of our desired
Process natural constituents from the available raw materials. There are
different types of extraction methods commonly used in industries
for the extraction of compounds from plant and animal sources, for
example, distillation extraction, solvent-based extraction, pressing
method, and sublimation process, which are categorized based on
their working principle. The reason behind the process of extrac-
tion of bioactive material is to get the therapeutically valuable
molecule and the inert part is eliminated with the help of a selective
solvent treatment known as the menstruum. Menstruum is the
solvent used in the extraction. The materials that remain after the
process of extraction are called “marc.” For the extraction process,
we need to prepare concentrations of raw materials using various
solvents. The solutions such as alcohol and hydro alcohol sols are
prepared from raw materials or chemical substances such as
belladonna [11].
Using various solvents with different polarities is the key feature
of this process. However, to date, there is no single extraction
method for extracting all the metabolites at a given time. Some of
the normal methods are listed as follows:
1. Maceration: In this method of extraction, the plant material is
crushed or chopped into small pieces. Sometimes the dried
Enzyme-Assisted Extraction 177
Table 2
List of bioactive compounds and their plant sources with uses
Table 3
List of the bioactive compounds derived from different fish species [10]
3 Process Development
3.1 The It is the crucial step in the process of getting the bioactive molecules
Disintegration of the out of cells. Cells are the basic unit of life; cells store valuable
Cell Wall by the Action bioactive compounds such as flavonoids, anthocyanin, carotene,
of Enzymes and many more which has significant value in both food and
nutraceutical industries; there is a variety of other classes of bioac-
tive compounds from medicinal plants, which have pharmacologi-
cal importance. Hence, it is important to extract them without
denaturation and also to increase the extraction yield and produc-
tivity. Therefore, as the science is developing, there are various
techniques that have been introduced for the easy extraction of
phytoconstituents from various sources. The enzyme-assisted
extraction is one such method that is commonly used nowadays
to better intracellular compound extraction methods.
During the process of extraction of intracellular compounds
from the cell, it is important to break open the cell so that it allows
the intracellular compounds to come out of the cell. The capacity of
the enzymes to degrade the cell wall component and also to disin-
tegrate the systematic integrity of the plant cell wall forms the basis
for enzyme-assisted extraction. When enzymes and substrates bind
to one another, the shape of the enzyme molecule adapts as better
as possible with the substrate to improve the interaction. The
change in form could put the substrate under strain and stress,
which could lead to the bonds breaking and speed up the reaction.
When the substrate concentration is high, the enzyme can acceler-
ate the process until the substrate concentration becomes limiting.
The operational characteristics of each investigation of enzyme-
assisted extraction are taken into consideration, including system
pH, enzyme extraction time, substrate particle size, concentration,
and reaction temperature. All study findings demonstrate that
enzyme-assisted extraction leads to a decrease in extraction time
and solvent volume in addition to an increase in yield and product
quality (Fig. 1).
Bioactive compounds in plants are secondary metabolites of
plants that have therapeutic or harmful effects on living things.
Secondary metabolites are created in plants in addition to the
basic biosynthetic and metabolic pathways for the substances
Enzyme-Assisted Extraction 181
Downstreat processes
Filtration
Step 3
• Bioactive compound extraction
Step 4
• Detection and separation compounds
Step 5
• Purification of compunds by Chromatography
Step 6
• Purified bioactive compound
182 Sadhana B. Maled et al.
3.3 Other Different Nowadays, the importance and commercial demands for the
Techniques Combined enzyme-assisted extracted bioactive compounds from plants are at
with EAE to Enhance a high rate. To fulfill the demands of the market, researchers are
the Extraction Process finding novel techniques, which are going to solve the problem
with high commercial value and usage. Some of the novel techni-
ques are microwave-assisted extraction, supercritical fluid extrac-
tion, and ultrasound-assisted enzymatic extraction. These
techniques are combined with enzyme-assisted extraction to
increase the efficiency of extraction to get more yield. These tech-
niques are eco-friendly and efficient with a high yield for the
commercial purpose to fulfill the demands of the market.
1. UAEE (Ultrasound-assisted enzymatic extraction):
Ultrasonic irradiation was utilized to expedite the treat-
ment of enzymes due to the increased effectiveness of
enzyme-used reactions and the convenience of practical work.
As innovative approaches for extracting bioactive compounds,
enzyme-assisted extraction methods linked with ultrasonogra-
phy have been devised [15]. Acoustic cavitation occurs when
ultrasound waves flow through a solvent solution, resulting in
increased extraction yield [16]. When ultrasonic waves are
exposed to a solvent media, tiny vapor-filled bubbles form. It
is named cavitation. Whenever the bubbles reach a particular
structure, they explode forming in localized high temperatures
and pressures. Whenever these bubbles break at the plant cells’
surface, the high temperature and pressure released create liq-
uid jets with shear forces that also are directed toward the plant
cells’ surface. The liquid jets and shear pressures that occur
during this procedure lead to physical harm to the cell’s wall
or cell membrane’s integrity. Ultrasound enhances cell wall
penetration, allowing more solvent to penetrate the cell wall
and leach compounds into the liquid phase. Furthermore,
under ultrasonic treatment optimal conditions (proper fre-
quencies and intensities) can result in increased enzyme work.
This is owing to favorable arrangement shifts and structural
rigidity, to facilitate bimolecular production [17].
Ultrasound-assisted enzymatic extraction is found to be
one of the easiest and quick methods of isolation. An indirect
sonication (ultrasonic wash) and also direct sonication, or
ultrasound horn can be used. The extraction yield in UAEE
of bioactives is related to factors such as ultrasound power
enzyme concentration. This technique will minimize the time
taken for extraction and can be inculcated in commercial use.
Enzyme-Assisted Extraction 183
3.4.1 Flavors and Colors Colors and flavors improve the quality of a food product by influ-
encing its visual appearance and taste. In the food sector, there is an
ever-increasing need for natural flavors and colors. Synthetic dyes
were suspected of emitting hazardous compounds that are highly
polluting, allergenic, carcinogenic, and toxic to humans. Given the
health and environmental concerns associated with industrial
chemical dyes, researchers redirected their focus away from artificial
(synthetic) colorants and toward the excitation of natural colorants
derived from plant sources [40]. Colorants taken from roots, bark,
foliage, nuts, berries, and flowers include anthocyanins, betalains,
chalcones, chlorophyll, carotenoid, and flavones. Traditional natu-
ral dye extraction procedures include water and alkali extraction,
fermentation, and solvent extraction. If the right enzymes are
chosen and the operating conditions are tuned, enzyme-assisted
extraction method has a lot of promise for pigment isolation. In the
past, commercially accessible enzymes including cellulase, amylase,
and pectinase were investigated. This method may hasten the
extraction of pigments through tough and compact plant matter
such as barks and roots. Conventional means of natural dye extrac-
tion, in addition to being time-consuming and ineffective, result in
the co-extraction of unwanted compounds such as chlorophyll and
waxes [41].
3.7 Advantages and The enzyme-assisted extraction method is a highly efficient tech-
Disadvantages of nique compared to the other extraction techniques as it takes very
Enzyme-Assisted less time with the high productivity of extracted compounds. It
Extraction Method requires the knowledge of the basic and simple methodology for
the extraction of compounds. The extracted compounds will retain
3.7.1 Advantages of their structural and physiochemical and configure stability during
Enzyme-Assisted and after the process of extraction. Consequently, the concept of
Extraction Method “green chemistry” is being pursued. People are searching for an
effective, ecologically friendly way to increase bioactive recovery
rates. Due to its improved extraction capabilities and environmental
friendliness, enzymatic extraction has demonstrated many benefits.
Through this process, we can exactly figure out our required intra-
cellular compound and can be extracted with high accuracy so that
purity of the extracted compound is enhanced. The process
required for the extraction of intracellular bioactive chemicals
using this unique technology is regarded as lenient, meaning
there are no precise requirements to be maintained. The cellular
barrier that is the cell wall, which processes cellulose, hemicellulose,
and pectin, can efficiently be degraded with enzymes, namely,
cellulase, hemicellulose, and pectinase, respectively, without affect-
ing the bioactives [54, 55].
3.8 Some of the (a) Antidiabetic activity: Diabetes is concerned with a group of
Pharmaceutical conditions characterized by a high level of blood glucose,
Activities of Bioactive commonly known as blood sugar [57]. Too much sugar in
Compounds the blood causes serious health problems, sometimes even it
may lead to death. In diabetics, there are two types: type 1 and
type 2. Type 1 diabetes destroys by the immune system by
mistake [58]. The reason is insulin binds to its receptor on
target cells; hence, less glucose is taken into the cells so that
more glucose stays in the blood. Therefore, this type of diabe-
tes is called insulin-dependent. Another type, known as type
2 diabetes, is characterized by insulin resistance. This condi-
tion is often associated with factors such as obesity, a sedentary
lifestyle, and an unhealthy disposition. Type 2 is related to
endocrine metabolism. In such circumstances, plants or natu-
ral products containing antidiabetic properties, such as insuli-
nogenic or secretagogue properties, hold significant promise
and potential for the development of novel pharmaceuticals.
There are so many plants with the antidiabetic properties.
Some of them are Acacia arabica, Aegle marmelos, agrimonia
eupatoria, allium cepa, Allium sativum, Aloe vera, Azadir-
achta indica, and Benincasa hispida [59]. The various parts
of medicinal plants can treat diabetes in various ways, includ-
ing insulin secretagogue activity, the insulin release from the
pancreas, insulin-like activity, an increase in plasma insulin
concentration, an increase in insulin binding to insulin recep-
tors, a decrease in plasma triglyceride levels, insulin-sensitizing
activity, and an antihyperglycemic mechanism to stimulate islet
insulin release [60]. Additionally, a sizable population world-
wide has switched to this complementary method of treating
illness because of its varied flora, affordability, and simplicity of
use with little negative effects. Studies show that medicinal
plants are multitargeting and least likely to fail during treat-
ment, which is supported by the evidence [61].
(b) Anticancer activity: Cancer is the result of uncontrolled, rapid
cell division. Numerous types of cancer can be found
[62]. Cancer is one the most deadly disease caused due to
metabolism. This disease is not completely curable. We can
just increase the life span of the patient with chemotherapy and
some antibiotics [63]. Presently, ten million people lose their
lives every year with this deadly disease, and this may exceed in
the future according to the WHO (World Health Organiza-
tion) [64]. Topoisomerase inhibitors such as irinotecan and
doxorubicin and alkylating drugs such as oxaliplatin, carbo-
platin, and cisplatin are used in chemotherapy. Irinotecan’s
adverse effects include neutropenia and sensory neuropathy
(side effects include nephron, gastrointestinal, cardiovascular,
196 Sadhana B. Maled et al.
4 Conclusion
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Abstract
In recent years, several innovative extraction procedures have been developed to carry out more effective
and sustainable extraction of bioactive compounds. Sustainability is a vital concept for social, technological,
and economic advancement, which strives to establish a circular economy. Thus, the significance and
demand of eco-friendly methods used for producing plant extracts is currently booming. However, the
food industries are strictly expected to implement manufacturing techniques that are highly effective and
energy-efficient because of the rising cost of energy and other utilities. Pulsed electric field (PEF) processing
is very efficient, more eco-friendly and sustainable compared to conventional extraction techniques such as
solvent extraction and steam distillation. Further, PEF is also a desirable and effective nonthermal method
with improved functioning, extractability, and retrieval of phytochemicals with nutritional benefits. Thus,
swapping the conventional techniques with PEF can minimize or eradicate the utilization of harmful
solvents and utilize less energy and water, and in return preserve the environment for the future genera-
tions. Therefore, PEF extraction technology has been considered as a sustainable strategy and green
technology to extract the bioactive compounds. Additionally, cutting-edge nonthermal extraction techni-
ques such as PEF make it intelligible and more effective to identify, characterize, and analyze bioactive
components. PEF also has various advantages when compared to conventional extraction techniques such
as cost efficiency, reduced extraction times, and greater yields with less solvent use. This chapter focuses on
the employability of pulsed electric fields as a suitable green technology for bioactive extraction.
Key words Pulsed electric field, Green technology, Nonthermal processing, Novel extraction tech-
nique, Bioactive compounds
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_9,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
201
202 Radhika Theagarajan et al.
Voltage Voltage
Sample transport
control device power supply
system
Treatment Treated
Samples
chamber samples
Temperature Temperature
inductors control system
4.1 Mechanism of The application of rapid pulses (μs to ms) of moderate electric
PEF-Based Bioactive voltage (usually 0.5–20 kV/cm) to a suitable substrate situated
Extraction Unit between two electrodes is known as the pulsed electric field
(PEF)-assisted extraction. The method has been used for preserva-
tion, enzyme, and microbial inactivation using high electric voltage
(5–50 kV/cm). Particularly, in cell cultures and plant systems, low
to medium PEF treatment intensities are frequently regarded as an
efficient pretreatment technique for improving secondary metabo-
lite extraction yields.
In the batch system of the PEF technique, the electric field
intensity ranges from 100 to 300 V/cm, and in the continuous
mode of extraction, it ranges from 20 to 80 kV/cm. Several
hypotheses share two points of view regarding the putative PEF
mechanism. One involves accelerating chemical reactions compris-
ing numerous substances in the biological cell membrane to
increase the solvent’s solubility, and the other is the electroporation
process (Fig. 3). An external electrical force is used in electropora-
tion or electro-permeabilization to increase the permeability of cell
membranes. A high-voltage electric field is positioned between the
electrodes and food or any other targeted materials. By generating
hydrophilic holes, which activate protein channels, the cell mem-
brane is pierced. When high-voltage electrical pulses are applied to
the sample, a force per unit charge known as the electric field
occurs. When high-voltage electrical pulses are applied across the
electrodes, the sample feels a force per unit charge known as the
electric field. When the membrane no longer serves as a structural
component, the plant material is removed [14].
Pulsed Electric Fields as a Green Technology for the Extraction. . . 207
4.2 Design and The main PEF variables were intensively evaluated to determine the
Fabrication of PEF- optimal PEF for the specific system to achieve the maximum poly-
Based Bioactive phenol content of the extracts. For specific extraction duration, it
Extraction Unit was shown that the key PEF parameters that affect permeability are
field intensity, pulse duration, and pulse period. For electropora-
tion, the uniform electric field chambers expose each cell in the
sample to the same electric field. High-yield intracellular chemical
extraction is feasible when the field strength is sufficient and close
to the ideal value. Due to the possibility that the best extraction
yields could differ noticeably above or below the ideal value, the
electric field strength set point must be determined by systematic
experimental design [15]. Figure 4 shows the schematic represen-
tation of an ordinary PEF-based processing system for the treat-
ments of food systems.
For instance, in a study conducted by Zhu et al. [16] PEF
pretreatment for protein extraction was performed with a PEF
generator system that was self-built, Cardamine violifolia was pre-
treated with PEF. A peristaltic pump was used to pump 4 g of
sample, dissolved in 120 mL of water, at a rate of 1.35 mL/s into
the treatment chamber. The operating parameters were as follows:
The frequency was 1.01 kHz, the half-peak width was 48 s, and the
pulsed electric field strength was 6.67 kV/cm. After six cycles, a
NaOH solution was used to bring the pH value to 9.0 ± 0.2, and
the treated solution was then extracted using conventional extrac-
tion (CE), ultrasound (US)-assisted extraction. After extraction,
the extracts were centrifuged at 4000 rpm for 20 min at room
temperature to get the supernatant.
Similarly, in a study performed by Athanasiadis et al. [17] 4.0 g
of freshly cleaned plant material (not dried) was crushed into
smaller pieces and combined with 80 mL of the solvent (at a ratio
208 Radhika Theagarajan et al.
Trigger signal
Control and
High voltage Energy
monitoring Power switch Pulse forming
DC supply storage
system
Fig. 4 Schematic representation of a typical PEF-based processing system for the treatments of food
application [7]
4.3 Configuration The high-voltage pulses are delivered to the treatment chamber
and Requirements of containing the food sample using a pulse modulator. To transmit
PEF-Based Extraction the stored energy in an economically sound way, power switches are
Unit required. Most significantly, it has an impact on the electrical sys-
tems’ overall design. Initially, various food sample components
were extracted using batch devices with PEF pretreatment (for
solid-liquid extraction). However, Yin et al. [18] successfully
applied extraction in a continuous-flow treatment chamber. Since
then, there has been a considerable advancement in technology that
resulted in the invention of a continuous PEF extraction system,
making it simpler to extract continuous products. According to
reports, the PEF continuous extraction system has efficiently
extracted fishbones, eggshells, tomato juice, and other materials
[19]. However, it has not been widely implemented in food
Pulsed Electric Fields as a Green Technology for the Extraction. . . 209
Cooling
coil
Pump
Untreated Treated
Generator of
product product
high voltage
pulse
4.4 PEF—Batch and The treatment chambers can be separated into batch treatment
Continuous Treatment chambers (Fig. 6) and continuous treatment chambers (Fig. 7)
Chamber based on the type of the treated product (solid, semisolid, liquid,
and semiliquid). The latter form is far more practical for
manufacturing applications since it enables the pumping through
the chamber of liquid and semiliquid products. A central computer
manages the process. It sets the parameters, manages the operation
of the pump, and collects data from the sensors inserted within the
chamber. The main issue with liquid products handled with PEF is
the nonuniformity of the electric field distribution inside the treat-
ment chamber, which is brought by the design of the chamber, the
occurrence of bubbles and other contaminants, and the thermo-
physical characteristics of the product itself. As a result, some areas
210 Radhika Theagarajan et al.
Control Panel/
PEF Generator Data Processing
Electrodes
Sample to be Placed/
PEF Chamber
Oscilloscope
Pump Flowmeter
Thermometer
Cell fusion
Cell destruction
Treatment intensity
Fruits and Phenolics, total Blueberry fruits (Vaccinium EF: 1–5 kV/cm 10 Hz P: 1–23 μs 50% ethanol; T: 20 ± 1 °C [13]
vegetables anthocyanins, myrtillus L.) E: 10 kJ/kg 0.5% HCl, v/v
and antioxidant
activity
Carotenoids, Date palm fruit extract EF: 1, 2, and 3 kV/cm 10 Hz N: 30 t: 100 s [3]
anthocyanins,
flavonoids, and
phenolics
Polyphenols Grape vine (Vitis vinifera); Greek EF: 1.2–2.0 kV/cm P: 10 μs t: 1 ms [22]
mountain tea (Sideritis scardica)
and Saffron crocus (Crocus
sativus)
Phenolic Cocoa bean shell and coffee silver EF: 1.5–3 kV/cm for N: 500–1000 S: water for CBS; t: 5–20 μs [23]
compounds skin CBS and ethanol/water
1.30–4.40 kV/cm solution for
for CS CS
Phenolic Brewers’ spent grain EF: 2.5 kV/cm 50 Hz P: 10 μs, N: Ethanol/water t: 14.5 s [24]
compounds 500–2250
Phenolic Onion 2.5 kV/cm 1 Hz 90 pulses Water 45 °C [25]
compounds and 100 μs
flavonoid
compounds
TPC, AA, and total Blackcurrant 1318 V/cm 315 pulses Cold pressing 10 and 22 °C [26]
monomeric
anthocyanins
(continued)
Pulsed Electric Fields as a Green Technology for the Extraction. . .
213
Table 1
214
(continued)
Treatment intensity
Pigments Betanin and Red beetroot tissue P: 4.38 kV/cm 10 μs Acidic buffer 9.2 °C. [27]
vulgaxanthin E: 4.10 kJ/kg 10, 20, 30 (pH: 6.5)
Turmeric crude Rhizomes of turmeric 0.5–7.5 kV/cm 100 ms 20 ms [28]
extracts
Pigments Spirulina 30 kV 300 Hz 4–32 μs [29]
Radhika Theagarajan et al.
Green leaves Polyphenols Olive leaves 1 kV/cm 1000 Hz 1000 μs Aqueous ethanol 30 min [30]
Phenolics Fresh rosemary and thyme 1.1 ± 0.2 kV/cm 10 Hz 67 bipolar Aqueous NaCl 40 °C [31]
by-products pulses of
30 μs
Bioactive Custard apple (Annona squamous) Electric field strengths 100–300 Ethanol (70%, 2.5–5 min [32]
compounds leaf extract (2–6 kV/cm) pulse pulses v/v)
energies (45–142 kJ/
kg)
Antioxidant Drumstick (Moringa oleifera) plant 7 kV/cm 37 kHz Aqueous 40 min [33]
activity extraction
By-products Nonpurified Peach pomace waste 0.8–10 kV/cm 0.1 Hz 4–30 Ethanol: water 20–22 °C [34]
bioactive monopolar 70:30
extracts pulses of
4 μs
Total phenolic Cocoa bean shell (CBS) and coffee 1.5–3 kV/cm 50 Hz 500–1000 0.1% formic acid 5–20 μs [23]
contents silver skin and 100%
methanol
Polyphenol and Grape stems 1 kV/cm 1 Hz 30 min [35]
volatile
compounds
Phenols, Fresh thinned peaches EF: 0–5 kV/cm 1 Hz P: 30–150 μs Water t: 3 μs [36]
flavonoids, and E: 0.61–9.98 kJ/kg N: 10–50 T: 15–35 °C
antioxidant
compounds
Algae Polyphenols and Brown macroalga (Alaria esculenta) 0, 720 pulses Ethanol [37]
carbohydrates concentration
(0%, 15%)
Starch Green macroalga (Ulva ohnoi) 1 kV/cm 3 Hz 200 pulses [38]
Phycocyanin and Spirulina platensis 15–25 kV/cm 2–6 Hz 1 μs [39]
protein
Pigments and total Tetraselmis chuii and Phaedoactylum 1–4 kV/cm 2 Hz 45–400 pulses Aqueous or 100 ms [40]
phenolic tricornutum 100 kJ/kg dimethyl
compounds sulfoxide
(DMSO)
Pulsed Electric Fields as a Green Technology for the Extraction. . .
215
216 Radhika Theagarajan et al.
Integrated
Commodity Bioactive compounds treatment Treatment conditions Significant findings Reference
Canola seed Total phenolic content, Microwave and Microwave: Liquid to soil ratio of 6.0 and 633.3 W Due to their reduced solvent usage, shorter [44]
cake total flavonoids PEF for 5 min extraction times for moderate microwave power,
PEF-assisted extraction: 30 V, 30 Hz, 10% ethanol lower electroporation voltage and frequency, and
concentration and 10 s greater efficiency in extracting polyphenols
Almond Condensed tannins, PEF and US PEF: Flow rate of 40 mL/min, 18 kV/cm electric Permeabilization, increases the yield, extraction [41]
extract anthocyanin, total field strength for 500 L/s, 1 kHz pulse frequency; efficiency, and the extraction of intracellular
phenolics, total US: 40 kHz ultrasonic frequency, 200 W radiation, metabolites. Due to the release of bound
flavonoids and 35 °C temperature for 20 min phenolics mediated by cavitation-induced cell
membrane rupture, ultrasound improves the
bioactive component
Grape stem Polyphenols PEF and US PEF: low electric field strength of 1 kV/cm Compared to solely ultrasound-assisted extraction- [35]
(30 min). derived extracts, this integrated technique helps
US: 35 kHz frequency and a 320 W high frequency to improve the yield of volatile compounds in the
peak extracts
Spirulina Phenolics, chlorophyll, and PEF and PEF: 44 pulses, 3 kV/cm, 99 kJ/kg PEF has the power to damage the structural and [45]
carotenoids pressurized PLE: preheating time of 1 min, heating time of functional integrity and obliterate the
liquid 5 min, flush volume of 60%, nitrogen purge time microalgae’s adherent filaments, which helps to
extraction of 60 s, extraction pressure of 103.4 bars, facilitate more effective PLE extraction. The
(PLE) extraction temperature of 40 °C, extraction time polyphenol content is increased by this integrated
of 15 min technique (PEF + PLE)
Ziziphus lotus Total phenolics, Supercritical fluid – Extraction of pharmaceutical drugs and nutritional [46]
fruits, chlorophyll, and extraction and supplements from natural sources, such as
leaves, and carotenoids PEF aromatic and medicinal plants, spices, and herbs
roots
Pulsed Electric Fields as a Green Technology for the Extraction. . .
217
218 Radhika Theagarajan et al.
10 Conclusions
The demand for natural products extracted from plants and other
materials is booming, especially for those nutrients derived from
by-products, as a result of customers’ concerns about conceivable
hazards in the extracts and health risks associated with employing
organic solvents as an extraction medium. Therefore, researchers
are increasingly focusing their attention on investigating more
complex and efficient green-extraction processes as a result of the
rising demand for sustainably extracted bioactive compounds. Like-
wise, PEF technology is a recently developed nonthermal method
that has been mainly used in the food industry for various applica-
tions. The PEF procedure used to extract bioactive and nutraceu-
ticals has evolved recently. Moreover, the dielectric breakdown
theory is the chief principle for bioactive extraction on a theoretical
basis using PEF and is one of the widely recognized mechan-
isms. There has not been much research conducted on the mecha-
nism underlying PEF dependent bioactive extraction, however,
these techniques have been used as assisting technique for the
improved extraction.
220 Radhika Theagarajan et al.
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45. Zhou J, Wang M, Berrada H, Zhu Z, Grimi N,
Barba FJ (2022) Pulsed electric fields (PEF),
Chapter 10
Abstract
An efficient nonthermal food processing method is called pulsed electric field processing. It involves
applying a short-duration, high-voltage pulse to a food product that is sandwiched between the two
electrodes. This method is used for microbial inactivation in food, making them last longer without the
need for preservatives or thermal treatments. This method results in many benefits for foods, such as
protection of their original nutritional value, taste, color, freshness, and flavor. Apart from these common
benefits, there are many other benefits of pulsed electric field (PEF) for specific foods. The PEF treatment
can increase the number of bioactive substances that can be extracted from plant tissues and their
by-products, including vitamins, minerals, polyphenols, anthocyanins, and plant oil, as well as the soluble
intracellular matter from microorganisms. In this chapter, we examine how the PEF method is used in the
extraction of bioactive compounds as well as their applications in the food and nutraceutical industries.
Key words Pulsed electric field, Nonthermal, High-voltage pulses, Extraction yield, Microbial inacti-
vation, Bioactive compounds, Intracellular matter
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_10,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
223
224 Subrahmanya Hegde et al.
Solvent
Bioactive compound
Fig. 1 Cellular disintegration and the extraction of bioactive compound from the ruptured cells upon the
application of pulsed electric field
To achieve this complex process, that is, the high voltage at a very
short interval of time, engineers have designed equipment that has
all the necessary components to meet our required purpose. The
entire unit of PEF consists of a generator that produces very high-
voltage pulses, a monitoring and control system, and a fluid man-
aging assembly with a treatment chamber. To convert alternate
Pulsed Electric Field Extraction 227
3.1 Batch Method of In the batch method of extraction, the unit contains a pretreatment
PEF Extraction chamber for solid-liquid extraction. The cylindrical vessel of poly-
propylene is fixed in the pretreatment unit of PEF. It consists of two
electrodes made of stainless steel, which are parallelly arranged, and
the distance between them is 10 mm. Electrical field strength, shape
228 Subrahmanya Hegde et al.
number, the width of the pulses, and frequency are the most
important parameters one should consider during processing [5]
(Fig. 3).
5.1 Tissue The effects of electroporation depend on the physical and chemical
Parameters characteristics of the cell and the tissues, such as the composition,
thickness, and size of the cell membrane. The value of the trans-
membrane potential depends on the type of tissue and the rigidity
of the membrane; it is inversely proportional to the size and rigidity
of the cell. Soft plant tissues typically require a moderate strength of
the electric field, whereas hard tissue parts require a comparatively
high amount of electric field strength to rupture the cell membrane
by exceeding transmembrane potential. The larger field strength
necessary is 20 kV/cm, and the moderate quantity of electric
strength required is (E 5 0.12 kV/cm) [15].
5.2 Media Parameter According to certain research, the medium’s conductivity and ionic
potential may have an impact on the membrane’s ability to separate.
According to existing lines of evidence, the conductivity of the
medium is inversely proportional to cell mortality in the case of
microbe inactivation and gene transfection. However, several inves-
tigations have shown the exact opposite phenomenon. In extrac-
tion studies, the medium’s conductivity is generally unaffected. The
plant tissues or dietary by-products do, however, contain large
amounts of extracellular ionic compounds (salts) when suspended
in the aqueous environment during PEF treatment, which may
change the cell size (owing to osmosis) and electrical conductivity.
The heat generated during the PEF treatment may have a favorable
or negative effect on extraction efficiency. Larger field amplitude
pulses can be employed in low-conducting mediums to achieve the
appropriate level of electroporation [14].
5.3 Pulse Parameter The degree of electroporation may be influenced by the pulse’s
electric field strength, polarity duration, and frequency. For paral-
lelly arranged electrodes, the electric field strength can be defined as
the ratio of voltage and the distance between the two parallelly
arranged electrodes.
Pulsed Electric Field Extraction 231
6.1 What Are Secondary metabolites of plants that have medicinal or toxic effects
Bioactive Compounds? on living organisms are known as bioactive substances in plants. In
addition to the primary biosynthetic and metabolic pathways for
compounds related to plant growth and development, secondary
metabolites are produced in plants. These by-products of plant cells
are not required for daily plant function, but some of them are
found to have important functions in living plants, including sig-
naling and protection. The majority of plant species appear to be
able to produce these substances. But some of the chemicals and
bioactive compounds from the plants have pharmacological and
toxicological effects on humans and animals [21].
Plants are a large reservoir of various kinds of bioactive com-
pounds; these are the extra constituents that are rich in nutritional
value. Therefore, it is important to utilize these compounds in
232 Subrahmanya Hegde et al.
Table 1
Utilization of the PEF method in the extraction of bioactive compounds from various sources
S. Bioactive
No compound Product The optimum value of the PEF application References
1. Polyphenol Red grape E-400 V/cm, n-2 tp -2000+_1 μs, delta [31]
pomace t-20 ms [32]
Orange juice E-35 kV/cm, f-800 Hz, tp-4 ms, tPEF- [33]
Orange peel 750 ms [34]
Tea leaves E-5 kV/cm, n-20, tp-3 μs, tPEF-60 μs [35]
Green grapes E-0.9 kV/cm, tPEF-0.5 s μs
E-10 kV/cm, tPEF-100 μs, n-15
2. Anthocyanin Merlot grapes U-7 kV, f-178 Hz, tPEF-150 s [36]
Raspberry E-3 kV/cm, tPEF-15 μs, n-420 [2]
Potato E-3.4 kV/cm, t-3 μs, n-35 tPEF-105 μs, [37]
Red cabbage 8.9 kJ/kg [38]
Blueberry E-2.5 kV/cm, tPEF-15 μs, n-50, [39]
W-15.63 J/g
E-3 kV/cm, W-10 kJ/kg, f-10 Hz, tp-20 μs
3. Carotenoids Carrot E-0.6 kV/cm, tPEF-3 ms, tp-20 μs, f-5 Hz [40]
Tomato E-25 kV/cm, tPEF-110 μs [41]
Orange juice E-35 kV/cm, f-800 Hz, tp-4 ms, tPEF- [42]
750 ms
4. Lycopene Tomato E-1.5 kV/cm, n- 40, tp- 500 μs [43]
Watermelon E-35 kV/cm, f- 200 Hz, tp- 50 μs [44]
5. Lutein Microalgae E-25 kV/cm, tPEF-150 μs [45]
6. Alkaloids Korean E-20 kV/cm, n-8, tPEF-60 s [46]
monkshood E-0.75 kV/cm, tPEF-600 μs [47]
Potato peel
7. Betulin Mushroom E- 40 kV/cm, tp- 2 μs [2]
8. Protein Microalgae E-38 kV/cm, f- 158 Hz, tp-232 μs [2]
9. Polysaccharides Corn silk E-30 kV/cm, tp- 6 μs [48]
10. Lipid Microalgae U-45 kV, E- 45 kV/cm, tp-10 s, [49]
tPEF-30 s, n-3
234 Subrahmanya Hegde et al.
6.2 PEF-Assisted Fruits and vegetables are the reservoirs of valuable antioxidants,
Extraction of Bioactive minerals, vitamins, and fiber [50]. These contain beneficial antiox-
Compounds from idants such as phenolics, carotenoids, and anthocyanin [51].
Fruits and Vegetable Hence, these compounds have commercial and medicinal impor-
Sources tance, and it is necessary to extract them. To achieve this, PEF
method plays an important role in the extraction process. There
are various other types of traditional methods of extraction of
bioactive compounds such as the Soxhlet extraction method, mac-
eration techniques, and hydrodistillation [52]. However, all these
methods are time- and energy-consuming and are also less produc-
tive. Various studies have been undertaken to compare the extrac-
tion yield between normal extraction methods and PEF-assisted
extraction methods. In all the cases, the PEF-assisted extraction
gave the best result compared to normal traditional methods. One
of the study findings showed that PEF-assisted extraction has
improved the release of vitamin C, anthocyanin, and also increased
antioxidant property of the grape juice when compared to the
normal untreated sample [2, 5, 53]. Hence, the extracted sample
had a good composition of phytochemicals and helped to prevent
the oxidation stress of the cell [53].
Another study accounts for good quality extraction of phenols
and flavonoids from onion through PEF extraction. As the cells
have a plasma membrane, which affects the mobility of intracellular
substances among other cells, it is a difficult and time-consuming
process to extract the required compounds by traditional methods
of extraction. However, in contrast, in the PEF method, the high-
voltage pulses will cause a plasma membrane permeability by form-
ing a pore so that the substance inside the cells can be easily
removed out, leading to high yield in a short interval of time [54].
Similar studies show that the PEF extraction method provides a
greater yield of polysaccharides, proteins, and polyphenolic com-
pounds from white button mushrooms when compared to usual
thermal treatments [5].
6.2.1 From Plant Leaves One of the research studies has been done by Khursheed Ahmad
Shiek and his team about the examination of extraction yield of
bioactive compound from the leaf of custard apple. They prepared
the extraction by adding 70% of ethanol along with the help of a
pulsed electric field. Results showed the increased cell integration
index in the extraction of custard apple when they provided a pulse
electric field of 6 kV/cm of about 300 pulses with the energy of
142 kJ/kg for about 5 min. They also found that the productive
yield of extraction through the PEF method has shown an addi-
tional higher percentage of 5.2% than those of untreated extracts by
the PEF method, which is 13.28%. The concentration of chloro-
phyll A and B in the pulsed electric field–treated custard apple leaf
extraction was found to be very less or negligible [55].
Pulsed Electric Field Extraction 235
6.2.2 Extraction of There is a variety of seeds from different plants that have numerous
Bioactive Compounds from beneficial applications in the day-to-day life as well, as they have
Plant Seeds commercial and medicinal importance. The seeds include ground-
nuts, cotton, safflower, and sunflower. These are the most impor-
tant commercially valuable seeds as they are the reservoir of oil and
fat [57]. These fats and oils contain triacylglycerol, which plays a
vital role in enhancing the immune system of the body [58];
moreover, these oils are the main source of calories and vitamins.
Usually, the oil from these seeds is extracted by squeezing the seeds.
Once the oil is extracted, the press cake is then subjected to solvent
extraction. This is usually done by normal Soxhlet extraction meth-
ods by using a large quantity of hexane [59]. However, nowadays,
the PEF extraction method is incorporated at an industrial level to
increase the extraction yield without any negative impact on the
nutritional value of the product [5, 60].
Studies show that from the PEF extraction method oil yield of
55.9% from sunflower seeds [5], an yield of 0.105% with a 50%
increase in essential oil from damask rose flower seeds [5], 48.24%
with hexane (40 mL) solvent from sunflower seeds, [55] 22.66 kg/
100 kg from Arroniz variety of olive fruit seeds, [61] and 85.5% oil
yield from Nocellara del Belice variety of olive fruit seeds [62].
6.2.3 Extraction of Soxhlet extraction is the most popular approach for obtaining
Bioactive Compounds from bioactive compounds from plant sources. Other classical extraction
Herbs and Spices methods include maceration, etching, and cohobating. However,
the commercial production of essential oils has historically relied
236 Subrahmanya Hegde et al.
6.2.4 Extraction of Microorganisms, including bacteria, yeast, and algae, are excellent
Bioactive Compounds from sources of extremely valuable substances such as enzymes, pig-
Microorganisms ments, and nutrients. Since the majority of these chemicals are
found inside the cell, it is crucial to isolate and refine them before
using. Microorganisms are capable of a wide range of reactions and
may adapt to a broad spectrum of environmental factors. They can
be introduced into the laboratory from nature to build advanta-
geous molecules using inexpensive materials such as carbon and
nitrogen. Bioactive compounds produced by bacteria are extremely
advantageous for human nutrition and health due to their
biological activity. The screening of naturally occurring microbial
products for the creation of novel medicinal medicines has
advanced in research [65].
Several studies have shown that PEF-assisted extraction of
bioactive compounds from various microorganisms, such as
Arthrospira platensis, fresh abalone (Haliotis discus hannai Ino)
viscera, fresh microalgae Auxenochlorella protothecoides studied,
which has resulted in increased extraction of
151.94 ± 14.22 mg/g, 42.35%, 175.20 mg/100 mL, and 97%,
respectively [66–68].
6.2.5 Extraction of In the recent times, due to the increase in the population and the
Bioactive Compounds from discovery of various food products, there is also increasing in the
Food Wastes rate of food waste. Food waste may be agricultural, bakery, dairy,
and industrial; these food wastes are nowadays leading to different
types of pollution around the world. Hence, the scientists pro-
pound ways to reduce food waste and utilize them for beneficial
aspects. Most of the food wastes from agricultural and dairy foods
are a large reservoir of valuable bioactive compounds such as car-
bohydrates, phenolic acids, flavonoids, anthocyanin, terpenoids,
limonoids, lipids, catechins, tannins, vitamins, alkaloids enzymes
such as amylase, cellulase, pectinase, and invertase. Hence, it is
important to extract those valuable bioactive compounds without
simply discarding them. Conservation of energy and production of
energy are the need of the hour. As science and technology have
developed, scientists have invented many extraction methods,
Pulsed Electric Field Extraction 237
Table 2
Bioactive compounds from fruit wastes
Name
of the fruit Waste type Bioactive compound extracted References
Citrus fruits Peel, seeds Carbohydrates, limonoids [69, 70]
Apple Pomace Carbohydrates, phenolic acids, flavonoids, anthocyanins, [70–72]
dihydrochalcones, triterpenoid
Mango Kernel seed Flavonoids, phenolic acids, tannins, xanthanoids, catechins, [70]
Peel hydrolysable
Carotenoids
Banana Peel Flavonols, catechins, catecholamines, phenolic acids [70]
Elderberry Branch waste Phenolic acids, flavonols, anthocyanins [70]
Table 3
Bioactive compounds from vegetable wastes [70]
Table 4
Bioactive elements found in dairy, marine, and animal waste products [70]
The demand for safe and high-quality food items has led to the
development of numerous unique food processing processes in
recent years. Consumers today have high standards for the items’
olfactory quality, usability, and nutritional worth. They also place a
high value on the utilization of environmentally sustainable food-
producing methods. The demand for products that resemble fresh-
ness and for food produced using environmentally friendly prac-
tices, as well as the growing customer interest in food with high
nutritional value, all stimulated the incorporation of pulsed electric
field (PEF) technology into food production [6, 73].
Pulsed electric fields (PEFs) have been utilized successfully and
safely on a range of different products in the food and bioproces-
sing industries. In Germany, Ukraine, and Moldova, the first stud-
ies on the use of pulsed electric fields (PEFs) were published in the
1950s, but it took decades for the technology to be used in indus-
trial settings. Since the 1990s, more than 20 research organizations
have been investigating the basic mechanisms of action, influencing
variables, and potential applications [74].
Applications of the pulsed electric field (PEF) can be used to
disintegrate biological tissues or microorganisms. There are many
uses for this technology, including improving mass transfer during
extraction or drying processes and mild food preservation. The
method has acquired its initial commercial uses. The reliability
Pulsed Electric Field Extraction 239
9 French Fry Manufacturing Saves Water and Energy by Utilizing the PEF Method
means that up to 10% less oil will penetrate the product. More than
90 PEF systems are currently in operation by the global fries
industry [76].
9.1 Perfect Vegetable chips are a fad, but it can be difficult to make them
Vegetable Chips consistently well. However, the use of PEF results in significant
quality improvements along the entire production chain: less starch
is discharged into the processing water, slicer blade wear is reduced,
and so on. Users of PEF also get from 1% to 2% yield boost. Quality
benefits range from better crunch to improved color to more of the
original vegetable’s natural flavor. PEF makes it possible to use raw
materials and shapes that were not before. Accelerated moisture
release following PEF permits lower frying temperatures in less
time, preserving the color of natural food while reducing the devel-
opment of acrylamide for products such as sweet potato, carrot,
parsnip, or beetroot chips [77].
10.1 Premium One of the earliest methods for preventing microbial development
Quality Drying and preserving a food product’s quality is drying. The process is
typically constrained by moisture diffusion. PEF removes this
restriction, enabling a decrease in temperature and a reduction in
drying protocol time as it opens the cell membrane. For the major-
ity of plant-based products, a drying time reduction of about 20% is
achieved because water may migrate from the product, preventing
the formation of a core crust and product shrinkage. Less adverse
effects on product color, shape, flavor, and energy savings result
from lowering the drying temperature. Additionally, PEF
Pulsed Electric Field Extraction 241
10.2 Peel Removal: PEF also has an impact on the structural qualities of plant matter.
The Easy Way Fruits, kernels, and seeds can vary in their elastic characteristics and
peel attachment after treatment. The tomato skin may be readily
removed without any connected tomato flesh following treatment
at 2 kJ/kg. Increased flexibility improves kernel integrity and
reduces breakage during shelling for nuts and seeds such as
cashews [79].
10.3 Superior Quality PEF not only affects microbial cells but also plant-based cells.
Juices Microbial inactivation results from the loss of membrane barrier
function in yeasts, molds, and bacteria. To ensure the juice’s micro-
biological safety and to provide a particular shelf life, the PEF
treatment reduces the microbial load of the juice. Reduced treat-
ment temperature and duration are the main advantages over tra-
ditional thermal processing. Thus, heat-sensitive flavors, colors,
and nutrients are unaffected. PEF can be run continuously and is
simple to integrate into existing processing lines, in contrast to
other nonthermal processing choices. The majority of industrial
PEF lines in the juice business use this technology since it works
well with mild temperatures. With inlet temperatures ranging from
30 to 40 °C and maximum product temperatures well below 60 °C,
the majority of industrial PEF lines in the juice industry employ
preheating and cooling systems that are already in place or that have
been specially designed for them. Compared to a high-
temperature, brief treatment, the temperature reduction—typically
more than one z-value—leads to a premium appearance and
flavor [80].
10.4 Use of PEF in Treating animal cells such as meat has positive impacts as well. PEF
Meat Processing modifies the structure of meat to make it more softer and delicious,
whereas tumbling mechanically can speed up the process. The
production process is more efficient and meat quality improves as
a result of the about 50% faster brine uptake following PEF treat-
ment of the meat [74].
the oral products that contain dietary ingredients that are meant to
enhance the flavor of the foods we eat. Mostly all these nutraceu-
ticals come from organic materials, mostly plants and microbes
[81]. “Nutraceuticals” is a term that is occasionally used inter-
changeably or in conjunction with the terms “functional foods,”
“bioactive chemicals,” “natural food additives,” and “dietary sup-
plements.” To give a variety of health benefits and to ward against
diseases, certain proteins, fatty acids, fiber, plant extracts, and sec-
ondary metabolites have been employed as nutraceuticals. The
global nutraceutical industry is constantly growing as a result of
the rising demand for functional foods and nutraceuticals, particu-
larly in industrialized nations. To develop nutraceuticals, businesses
are concentrating on mild and effective (in terms of productivity
and purity) technologies. Some of the important applications of
plant bioactive compounds in nutraceutical compounds are men-
tioned in Table 5 [14].
11.2 Extraction of According to some studies, PEF is used to extract various impor-
Nutraceuticals from tant chemicals from microalgae (Chlorella vulgaris, Chlamydomo-
Microalgae nas reinhardtii, and Dunaliella salina). In dietary supplements,
nutraceuticals, and food additives, lipids derived from microalgae
can be a valuable source of essential fatty acids. Some research
studies and patents have revealed the possible use of PEF for the
microalgae’s pretreatment to boost lipid production. After PEF
treatment, lipid droplets may remain inside cells. However, algal
lipids can be extracted with suitable solvents following the separa-
tion of other extractives [89].
Table 5
Plant bioactive compounds and their function and applications in nutraceutical industries [82–87]
hypocholesteremic, hypotensive
(continued)
Table 5
244
(continued)
11.3 Extraction of There are several bioactive compounds from plants that can be used
Various Bioactive as nutraceuticals and can be extracted through the various available
Compounds from extraction techniques including pulsed electric field extraction. The
Plants Having chemical compounds such as allicin from Allium sativum, betaine
Nutraceutical Value (trimethyl glycine) from green leafy vegetables and germinated
grains, bromelain from Ananas sp., capsaicin or trans-8-methyl-
N-vanillyl-5 noneamide from Capsicum annum, ellagic acid from
strawberries and raspberries, curcumin from Curcuma longa,
omega 3 fatty acids from Linum spp., and resveratrol especially
high in grape skin were extracted and are giving a huge contribu-
tion to the nutraceutical industries [82].
Flavones
Isoflavones
Flavonols
anthocyanins
Table 6
Bioactive compounds from animal sources and their application [83, 88, 91, 92]
Food
source Extracted bioactive compounds Function and benefits in nutraceuticals
Meat Fatty acids, minerals, vitamins, peptides Antioxidant activities and antihypertensive
Fish Proteins, fatty acids, polyether, peptides, Antithrombotic, immunomodulatory,
enzymes and lectins, polysaccharides antimicrobial, anticancer, and antioxidant
activities
Egg Avidin, ovalbumin lysozyme, ovomucin, Antimicrobial, immunomodulatory,
ovotransferrin, phospholipids antihypertensive, and anticancer activities
Milk Whey protein Helps to modulate both innate and adaptive
immune responses
15 Conclusion
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Chapter 11
Abstract
This chapter focuses on the case studies of the bioactive compounds that is defining the promising pathway
of compounds that can be used as functional units. This chapters allows to gain an insight of the steps taken
to make the optimization of the parameters and synthesis pathway. This chapter also focuses on the selection
of the material, sorting, and process of extraction. The highest percentage of bioactive compounds required
to achieve this extraction process and the point of consideration in implementation are also taken into
considereation A case study on polyphenols, alkaloids, and terpenoids will be discussed. This chapter
focuses on the novel extraction method by which an efficient amount of bioactive compounds are obtained.
The main focus is to explore the extraction of bioactive compounds from inexpensive resources or residues
that give cost-efficient products. Various novel methods of bioactive compound extraction and their
application in different domains will be discussed. This chapter provides a wholesome view of the steps in
the bioactive compounds by case studies and will carry forward to the novel extraction methods.
Key words Bioactive compounds, Polyphenols, Novel extraction method, Application, Case study,
Alkaloids, Terpenes
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_11,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
255
256 Muskaan Sharma et al.
solvent into a solid matrix, dissolution of the solute into the sol-
vent, diffusion out of the process from the solid matrix, and extrac-
tion of the solute [20]. In this process, the factor that comes into
the role is the diffusivity and solubility of the material that is
facilitating the extraction of the bioactive compounds. The law of
similarity and inter miscibility is the basic principle of extraction
protocol. The laws will be used to scale up the production of
bioactive in food industries and pharmaceuticals [21]. Extraction
is an advantageous process that is adding value to industrial growth.
The ongoing trend of bioactive compounds due to emerging con-
sumer needs will lead to the motivation to perform the new experi-
ment and optimize the process of extraction via nanocarrier [17].
2.1 Case Study 1: It has been evidenced that bioactive compounds comprise many
Fruit Seed-Based applications in the culinary industries as well as pharmaceutical
Bioactive Compounds industries. The long interest is in the functional feature of the
for the Formulation of diverse fruit seeds such as the tomato, guava, dates, as well as
Nutraceuticals apple. Some of the bioactive compounds in this include bioactive
peptides, lycopene polysaccharides, phytochemicals, and vitamins
[22]. These are abundant in fruit and its by-products and have
many health benefits. The role of bioactive compounds that are
obtained from the tomato and the seeds is that they are processed
into cans, products, and sauces. The seeds and the peels comprise
the bioactive compound named beta-carotene as well as lycopene.
They have a diverse phytochemical composition and the seeds of
tomatoes are known to be a natural source of antioxidants and
phenolic compounds and carotenoids. Another one is peel and
pulp which has lycopene, flavonoids, and phenolic acids. It can be
done by the methods of crushing, heating, and stirring. The con-
tent of moisture was 8.5%, fat was 20%, ash was 3.1%, and dietary
fiber was 35.1% in the tomato. When in the case study the phyto-
chemical analysis was done, the presence of the 14 flavonoids was
there such as quercetin, kaempferol, and isorhamnetin. They have
the power to alter many numerous cellular signal transduction
pathways as well as stimulation of endogenous defensive activities
are there [23, 24]. They have anticancer, antibacterial, antimuta-
genic, and stimulating endogenous defensive activities. They are
also known to have cardioprotective and antiplatelet properties. In
this case, there were many approaches used, such as the valorization
of unused parts in tomato, and there were methods for extraction
of the carotenoid compounds. The seed extracts of tomatoes have
antibacterial properties, and pharmaceutical and food sectors can
use them for the preservation of food and microbial deterioration is
there. The waste from tomatoes can be significantly used by indus-
tries to develop various by-products or functional foods, as well as
260 Muskaan Sharma et al.
2.2 Case Study 2: Pretreatment of seed will lead to the production of the phytosterol
Pomegranate Seed Oil composition. In addition, it holds the ability of antioxidant. For the
extraction of the bioactive compounds, seed oil is extracted with
the mechanical procedure. It will not lead to the effective results,
apart from this other extraction procedure will help. The extraction
procedure is known as the important step and it puts a great impact
on analysis as well as characterization. There are majorly four steps
that are used in food analysis such as sample preparation, data
acquisition, data analysis, and statistical integration. The sample
preparation and/or treatment, the extraction process, the extract
cleanup, and in most cases, extract concentration by evaporation
are all done in the first phase [26]. Depending on the purpose of
the study and the targeted analytes, the second stage involves the
collecting of data utilizing high-resolution analytical techniques,
such as gas chromatography-mass spectrometry (GC-MS), liquid
chromatography/mass spectrometry (LC-MS), and nuclear mag-
netic resonance (NMR). The equipment software processes the
data acquisition in the third stage. Depending on the goal of the
study, the final phase may include multivariate statistical analysis,
which might include, among other things, analysis of variance
(ANOVA), principle components analysis (PCA), partial linear
square analysis mixed with discriminant analysis, and cross-
validation. As per the case study, there are four strategies for the
treatment and extraction of the bioactive compounds from the food
matrices. It includes the treatment, in which the different methods
are milling, filtration, drying, hydrolysis, centrifugation, as well as
adjustment of pH. In the extraction part, analytes will be recovered
from the sample, and the classical advanced emerging techniques
are used. In the cleanup process, the elimination of the compounds
is done with the analysis. The different methods that can be used
include liquid-liquid extraction, dispersive solid-phase extraction,
as well as solid phase extraction. There are then advanced extraction
techniques that comprise microextraction techniques and these
comprise a wide range of applications. The different features are
Case Studies and Application of Different Novel Extraction Methods 261
2.3 Case Study 3: A The bioactive compounds are known to be found in fruit biowaste
Case Study of as well as they provide low-cost, integrated, and environment-
Raspberry Fruit friendly alternatives. The fruit named raspberry is known to be
Pomace—A Bioactive rich in antioxidant compounds which inculcate fiber, anthocyanin,
Compound and ellagitannins. The content of water is 80% and carbohydrates
are predominantly found. The chemical properties are dependent
on the edaphoclimatic conditions. The majority of antioxidants in
raspberry fruit pomace are squandered during juice manufacturing
(RFP). According to reports, RFP has 77.5% of the total nutritional
fiber found in fresh fruit [29]. The RFP also still contains a signifi-
cant amount of phenols. Tocopherols and -linoleic acid are both
abundant in the seeds. A sizable amount of biological potential is
also lost when RFP is wasted, including its antioxidant, antiproli-
ferative, and antihyperglycemic properties. Due to its capacity to
“spare” heat-sensitive chemicals, cheap cost, wide availability, and
efficiency, traditional maceration is the most widely used extraction
262 Muskaan Sharma et al.
3.1 Solvent In this extraction technique (HPLC), different organic solvents are
Extraction Technique introduced to effectively size the raw material that will take up the
desired components such as anthocyanins. These components are
preferring the properties of anticancerous agents and anti-
inflammatory [38]. For this, samples will undergo centrifugation
and then be filtered for the removal of the solid residues [39]. The
extract that is obtained is used as an additive, supplemental food,
and as an ingredient in functional food. Low processing cost and
ease of operation will be serving as the advantage over other
Case Studies and Application of Different Novel Extraction Methods 265
3.3 Subcritical Water This technique called the subcritical water extraction technique is
Extraction an alternative technology that is used for the extraction of the
phenolic compound from different food. Subcritical water also
refers to the temperature of the water which is between 100 and
374 °C, the pressure is also high and it is maintained in a liquid
state. The major advantage of the SCW over any other conventional
extraction technique is that it requires a short extraction time, the
solvent cost is low, the quality of extraction is high, and the major
advantage is that it is environment friendly. Subcritical water extrac-
tion and microwave-assisted technology is the most effective engi-
neering approach and also it offers some environment-friendly
techniques so several other plant components can be extracted
[46]. An author Tunchaiyaphum has extracted some phenolic com-
pound from the mango peels with the help of SCW technology.
The amount of phenolic compound, which is present in the mango
peel, was much higher than using the Soxhlet extraction technique.
Hence, SCW extraction is also known as an alternative green tech-
nology for phenolic compound extraction from agricultural waste.
It also substitutes the conventional method using the organic sol-
vent. There are mainly eight extracted phenolic compounds and
these are gallic acid, caffeic acid, chlorogenic acid, syringic acid,
protocatechuic acid, benzoic acid, p-hydroxyl benzoic acid, flavo-
noid, and coumaric acid [47].
3.4 Enzyme-Assisted There are a number of methods of enzymes that can be used for the
Extraction extraction of bioactive compounds from food waste. However, the
main source of extraction of the antioxidants is the plant tissue
[48]. The plant cells contain polysaccharides and these are hemicel-
lulose, cellulose, and pectins, all these act as barriers so the intracel-
lular substance can be released. There are several enzymes such as
cellulase, xylanase, beta-glucosidase, and beta-glucose held to
degrade the cell wall structure and then depolymerize the plant
cell wall polysaccharide [49]. As water is used as a solvent, in place
of chemicals, it is an eco-friendly approach that is used for the
extraction of some bioactive compounds along with oil. Several
bioactive compounds are released from the plant cell following
the cell disruption and extraction method. It also optimizes enzyme
preparation and it is done either alone or in the form of a mixture.
The enzyme-assisted extraction is a highly promising technique
when compared to conventional solvent-based extraction. It is
mainly the ability of the enzyme to catalyze the reaction, and mild
processing conditions should be used in an aqueous solution. It
leads to the production of high efficiency molecules that is cost-
efficient and organic rich [50].
Case Studies and Application of Different Novel Extraction Methods 267
3.5 Extraction with The extraction done with ultrasound is a relatively simple and
the Help of Ultrasound effective technique when it is compared to the traditional extraction
method. All the bioactive compounds are obtained from natural
products. The ultrasound method induces a much greater method
in which diffusion of the solvent in the cellular material is done.
Adopting this technique improves the mass transfer and along with
it disrupts the cell wall and facilitates the release of bioactive com-
pound. The amount of extraction is highly influenced by the ultra-
sound frequency, which mainly depends on the plant material
which needs to be extracted. Wang et al. [51] have demonstrated
the use of ultrasound-assisted extraction. In this method, the
extraction of three dibenzyl butyrolactone lignans, which are
trichloride, hemislienoside, and action, is done from Hemistepta
lyrate [52]. To determine the corresponding extract, high-
performance liquid chromatography is been done. In another
study by Fahmi et al. [53], the extraction efficiency of the four
isoflavone derivatives is studied; these are glycerin, daidzin, genis-
tin, and malonyl genistin from the soybean. To carry out this
extraction method mix-stirring method is used. As this technique
also used ultrasound, it has been known to improve the extraction
yield and it depends on the solvent. Azka et al. [54] have extracted
anthocyanins and other phenolic compounds from the grape peel.
This is also done using ultrasound technology as it takes care of
even the smallest details. Pineiro et al. [55] have optimized and
validated ultrasound-assisted extraction while extracting stilbenes
from grape canes.
Using this method, the stilbenes in the grape cane will be
extracted in 10 min. The temperature required will be 75 °C with
an ethanol concentration of 60% in the extraction solvent. From the
study, it was concluded that the grape cane by-product is a potential
source of the bioactive compound and it plays a vital role in the
food and pharmaceutical industry [56]. Aguilo Aguayo et al. [57]
also studied the effect of ultrasound technology while extracting
water from a soluble polysaccharide. These are obtained from the
milled and dried product which is generated from Agaricus bis-
porus. It has been observed that beta-Glucan has been obtained in a
specific amounts such as 1.01 and 0.98 g/100 g dry mass in the
particle size of about 355–250 and 150–125 μm, respectively; these
are the by-products of mushroom. The highest extraction was done
at 4.7% and this was achieved when there is an extraction time of
15 min, with an amplitude of 100 um and 1 h of precipitation in
about 80% ethanol [58].
3.6 The Microwave- This is a new extraction method that mainly combines microwave
Assisted and traditional solvent extraction. It is a highly advantageous tech-
Extraction (MAE) nique due to the short extraction time, high extraction rate, and
low cost of the traditional method. However, the major advantage
of ultrasonic-assisted extraction and solvent extraction is that the
268 Muskaan Sharma et al.
3.7 Pulsed-Electric This method is a highly novel extraction technology that is used for
Field-Assisted the extraction of bioactive compounds. This is a preferred method
Extraction (PEFAE) because less energy is required in it and also it is an environment-
friendly solvent. This method is a nonthermal extraction process, as
all the natural compounds can only be recovered at a minimum
temperature so quality and nutrition value can be obtained. Elec-
troporation is the primary mechanism that has been followed
behind the pulse electric field extraction method. In this process
of PEFAE, the electric energy is utilized to create nano- or micro-
poration of the cell membrane so all the bioactive compounds
which are present in the cell plasma can be extracted easily
[16]. An electric pulse is necessary for the transfer of the molecules
or the ions from inside the cell to the cell membrane as it acts like an
insulator [67].
In another study, it was observed that the apple peels were
treated by the pulsed electric field using several electric intensities
and time to extract the phenolic compound. The extraction is
analyzed using several electric conductivity and confocal laser
extraction. Results were obtained depending on the cell integration
index along with electric field intensity. This study has also con-
firmed that higher the intensity, the cell integration will be con-
stant, and the soluble matter recovery will be higher. Parniakov
et al. [68] has stated that the yield of the antioxidants, proteins, and
carbohydrates obtained from the mango peel was maximum when
PEFAE is at the intensity of 13.3 kV/cm. This process is carried out
with extraction at a 50 °C temperature for about 5 h at about
6 pH [69].
3.8 CE (Combination All the extraction technologies which are discussed above are men-
of Extraction) Process tioned and used in combination. When all the methods are used,
this reduces the extraction time, increases extraction yield, and
overcomes any limitation if present. The pre-treatment of any
fruit by-product by using the ultrasound or enzyme before any
CE process. Likewise, two or more emerging extraction processes
are used in combination such as UAE and SFE.
3.9 Interpretation Bioactive compounds are the type of chemical composition occur-
ring in plants and animals in small amounts. A required percentage
is needed for the efficient functioning of an individual. Bioactive
compounds are abundant in nature and considered superfoods.
The demand and growing interest of consumers lead to the inclina-
tion of the scientific community toward the discovery of versatile
compounds. To extract a single molecule from a plant source, a
series of steps is going to take place. This is a tedious process that
requires the sources and costs that make the availability of the
compounds to get restricted. At the same time, it is important to
overcome the restriction as the survival of an individual is depen-
dent on the consumption of bioactive compounds. Bioactive com-
pounds are comprising ample amounts of molecules that are
significantly contributing to the production of nutraceuticals. It
will act as the functional moiety in the variable industries whether
it is the food industry or pharmaceutical industry. Nutraceuticals
Case Studies and Application of Different Novel Extraction Methods 271
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sound in combination with other technologies
Chapter 12
Abstract
Pressurized liquid extraction (PLE), an advanced extraction technique, employs solvent extraction at
elevated temperatures and pressures, consistently under their individual critical points, so the solvent is
sustained in the liquid state during the entire extraction process. As a result of utilizing these exact
conditions of pressure and temperature, an alteration in the physicochemical properties of the solvent
arises. It is an alternative and advanced preparation technique compared to conventional extraction
methods in many areas, such as environmental, food, and pharmaceutical analysis. Medicinal plants are
the sources of numerous compounds that can tackle numerous diseases when they are used in a reasonable
combination. Every single plant contains one or more major bioactive compounds that are responsible for
various biomedical functionalities. This chapter summarizes the application of the PLE technique in
extraction and phytochemical analysis. The various advantages offered by this technique, such as low
solvent usage, less preparation time, high extraction efficiency and better reproducibility, have made it a
better alternative for the extraction and analysis of phytoconstituents.
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_12,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
275
276 Rakesh Barik et al.
1.1 Basic Principles The PLE method is a quick extraction technology due to the direct
of Pressurized Liquid interaction between the liquid solvent and the particles of the plant
Extraction (PLE) matrix under high pressure and subcritical temperature conditions
to extract the constituents of interest effectively. The efficiency of
the extraction technique mostly depends on the three correlated
facets of the matrix, mass transfer, and solubility. Related to the
matrix, its nature and the molecule of interest to be extracted and
its position within the matrix have an effect [7]. Elevated tempera-
ture significantly enhances solubility properties and mass transfer
between the plant matrix and the extraction solvent, resulting in
better extraction kinetics. Solvent viscosity decreases, facilitating
the plant matrix’s hydration and increasing the bioactive com-
pounds’ solubility. High temperature also causes the breakdown
of bonds or bonding forces in the matrix (dipoles, van der Waals,
and hydrogen bridges), facilitates the release of compounds, and
produces high extraction yields [8].
Pressurized Liquid Extraction for the Isolation of Bioactive Compounds 277
1.2 Mechanism and The PLE involves circulating the solvent through the extraction cell
Components of or column with a high-performance liquid chromatography
Pressurized Liquid (HPLC) pump where the plant matrix is placed to remove the
Extraction (PLE) bioactive molecules of interest [13]. The pretreated and
conditioned sample within the extraction column is exposed to
the designated temperature using an electrothermal liner while
being compressed to the specified pressure. In order to stabilize
the system and facilitate solvent diffusion through the plant matrix,
Pressurized Liquid Extraction for the Isolation of Bioactive Compounds 279
the pressure and temperature are kept constant, marking the begin-
ning of static extraction [14]. Afterward, the required pressure and
solvent flow rate are maintained, commencing dynamic extraction.
The extraction procedure is conducted through multiple cycles. At
the conclusion of the process, the extraction column containing the
sample is substituted with a new column consisting solely of an
inert element. The system is then cleaned by pumping out the
solvent and passing nitrogen or carbon dioxide through it [15].
As a result of the constraints posed by commercial equipment,
the only feasible method to handle liquid samples is by converting
them into solids, typically achieved through the addition of an
absorbent or adsorbent substance. The extraction process for ana-
lytes from semisolid and solid samples can be outlined using the
following five steps [16]:
1. Dampening of the sample (analytes to be extracted and matrix)
with menstruum
2. Dislodging of compounds from the matrix (including or not
the breakdown of chemical bonds)
3. Dissolution of the compounds in the menstruum
4. Dissemination of the compounds from the matrix
5. Propagation across the immediate solvent layer enveloping the
matrix, culminating in the bulk solvent
The extraction efficiency is contingent upon both kinetic and
thermodynamic factors. Consequently, the efficacy of extraction is
influenced by three interconnected facets [17]:
A. Matrix effect
B. Mass transfer
C. Solubility
The characteristics of PLE are subject to several factors that
impose limitations, including the careful selection of temperature,
pressure, flow rate, and extraction duration required for achieving
comprehensive extraction.
2 Instrumentation
Fig. 1 Representative diagram of a pressurized liquid extraction (PLE) system showing configurations for the
development of static system (a) and a dynamic system (b)
3.1 Effect of Temperature is the most important factor because it changes the
Temperature solvents’ physical and chemical properties and affects the extraction
efficiency. Temperature lowers the dielectric constant of the solvent
and changes its polarizability. It also reduces the viscosity and
density of the menstruum, enhances diffusion and penetration
Pressurized Liquid Extraction for the Isolation of Bioactive Compounds 281
into the matrix, and causes a higher mass transfer rate. Breakdown
of the structure of the vegetable matrix is brought about by high
temperatures, which reduces the surface tension between the men-
struum, sample, and the compounds during the extraction process.
This change is desirable to form cavities in the menstruum into
which the desired compounds are transported [21].
On the other hand, very high temperatures bring about the
degradation of thermolabile compounds. Too high temperatures
(>150 °C) may lead to the formation of toxic compounds such as
hydroxymethylfurfural (HMF) [22]. Hence, proper optimization
of temperature is essential after knowing the nature of compound
to be extracted, to avoid undesirable compounds, and get high
extraction yields [23].
3.2 Effect of Chemical affinity of the compound to be extracted for the extrac-
Menstruum tion solvent is the essential factor for proper selection of the men-
struum. This leads to high diffusion and mass transfer leading
further to high extraction yields. Additionally, the menstruum
should be nontoxic or less toxic in nature, inexpensive, accessible,
and easily disposable. The most environmentally acceptable solvent
system is the water–ethanol mixture [24].
3.4 Nature of the Plant matrices are usually subjected to unique treatments such as air
Plant Matrix drying, freeze drying, grinding, and screening before extraction.
Drying type and conditions directly affect the extraction yield. The
small size of the model makes it easy to change sizes. The larger
contact area of the material with the extraction solvent improves the
adsorption and separation of the target compounds. However, in
some studies, it is recommended not to reduce the particle size too
much in order not to prevent the diffusion of the solvent from the
compressed structure [27].It is also essential to know the nature
(nature and moisture) of the target compound in the plant matrix.
Many studies have shown that samples with high water content can
improve performance compared to dry models. This may be due to
cell disruption during drying, inhibiting the release of the target
compound. However, other studies have shown that water com-
petes with solvent extraction by reducing the recovery of bioactive
compounds in plant matrices [28].
282 Rakesh Barik et al.
3.5 Effect of The time the solvent is in contact with the matrix at a specific
Extraction Time temperature, pressure, and flow rate is the extraction time. Matrix
structure, type of target composition, temperature, pressure,
weight, etc. are some of the factors affecting its efficiency. Many
factors affect it. The static or dynamic extraction method is the
most specific parameter matrix to understand the extraction time
required to separate bioactive compounds from plants [29].
3.6 Impact of Energy The extraction process uses high pressure and temperature, which
and Environment means more energy. But it is lower than other extraction methods
such as supercritical fluid extraction or traditional Soxhlet extrac-
tion. According to some reported studies, the chemical effects
related to the type of solvent applied in the extraction of Rosemary
plants and Soxhlet extraction shows that PLE is less energy-
intensive than Soxhlet extraction. However, the temperature of
PLE is higher (183 °C vs. 78 °C for Soxhlet) [30].
3.7 Chemical and Pressurized liquid extraction using specific menstruum such as
Sensory Factors ethanol and others can produce some undesirable compounds
such as hydroxymethylfurfural (HMF), a nonenzymatic brown
indicator [31]. Similarly, HMF was associated with the induction
of colon cancer precursors in mice but was not toxic as found in
some laboratory tests. Ethanol concentration had a significant
effect on the overall performance of the PLE process. The lower
the ethanol content of the PLE extract, the higher the recovery of
phenolic acids and flavanols. Therefore, it is recommended to
recover at ethanol concentrations of 15%, 32.5%, and 50% for
phenolic acids, stilbenes, and flavanols, respectively. The extract
showed highest total polyphenol content and antioxidant activity
at 150 °C and 32.5% ethanol [32].
5 Applications
5.1 Isolation of Tocopherols were obtained from apple seeds and kiwi fruit using
Tocopherols this technique. A more pure extract was obtained, and the recovery
rate was similar to or higher than that of the existing method.
Extraction parameters optimized to maximize the effects of grain
tocopherols and tocotrienols or carotenoids from microalgae have
been described [36–38].
5.3 Estimation of Although the advantages of this technology have been reviewed for
Pesticides the study of biological and food samples, pressurized liquid extrac-
tion applications were initially focused on the extraction of envi-
ronmental pollutants [50]. Since this technique enables the
simultaneous extraction of many residue types with a wide range
of polarity, numerous applications for identifying pesticide residues
have been documented [51]. Thus, samples of animal and vegeta-
ble tissues are analyzed using pressured liquid extraction. Pesticides
are typically found in nonfat foods with a medium to high water
content, such as fruits, vegetables, and cereal-based diets. As a
result, it is frequently necessary to add a drying agent (such as
sodium sulfate or diatomaceous earth) [52, 53].
Pressurized liquid extraction has been used to identify a wide
range of pesticide residues in various agricultural and food matrices,
such as honey [54], organophosphorus pesticide residues in corn
[35], pyrethroid residues in feed samples [55], multiclass pesticide
residues in food commodities and grain, or herbicide residues in
soybeans [56].
By combining this method with gas chromatography/high
resolution isotope dilution mass spectrometry, common organo-
chlorine, organophosphorus, and pyrethroid pesticide residues in
herbal liquid extractions such as tea may be accurately
determined [57].
The analytical complexity of tea sample matrices can be reduced
by using pressurized liquid extraction followed by gel permeation
chromatography due to the high concentration of caffeine, pig-
ments, polyphenols, etc., in tea samples. Applying a selective pres-
sured liquid extraction technique, many pesticides as well as other
lyophilic pollutants can be recovered and identified from lipid-rich
matrices. The homogenized lipid sample is then placed in the
extraction cell on top of basic alumina, silica gel, and florisil. The
target chemicals are then extracted utilizing a single automated
process employing a 1:1 (v/v) dichloromethane/hexane ratio [58].
Pressurized Liquid Extraction for the Isolation of Bioactive Compounds 285
5.5 Determination of Metal and organometallic compounds have been determined using
Metals liquid extraction under pressure using Envi-Carb-based dispersing
agents and speciation of polar arsenic species in Seafood. The
recovery of four arsenic species was evaluated using silica, C-18,
sea sand, diatomaceous earth, and alumina as a cleanup agent. On
the other hand, Envi-Carb was used as a cleanup sorbent and
dispersing agent to extract Mg, Al, Ti, Cu, Ag, Sn, and Pb in
lubricating oils without any additional cleanup step [47].
5.6 Estimation of The release of pharmaceutical products into the environment has
Antibiotics raised issues concerning their occurrence, fate, and effects on the
biota. Antibiotics are an essential group of pharmaceutical products
widely used in human and animal health care, which are reportedly
ubiquitous compounds in the aquatic environment. Pressurized
liquid extraction is a reliable technique for extracting antibiotics
and other drug residues associated with suspended solid matter
[63]. Multiresidue analysis of sulfonamide antibiotics and their
acetylated metabolites in soils and sewage sludge can be performed
using fully automated pressurized liquid extraction methods [64].
In these methods, a subsequent step for preconcentration and
purification is required. The extraction of quinolone and
286 Rakesh Barik et al.
5.7 Standardization Pressurized fluid extraction is one of the most widely used techni-
of Polyphenols ques for extracting polyphenolic compounds from various sources
such as food, vegetables, seafood, and agro-industrial by-products.
Whether acidified or not, the hydrogen ethanol mixture (EtOH
> 50%) is the preferred solvent for the extraction of polyphenols by
liquid extraction. In addition, the temperatures of heat- and cold-
resistant phenolics are generally 40–60 and 75–220 °C,
respectively.
One study [62] used an optimized pressurized liquid extraction
to extract antioxidant phenoliccompounds from defatted peanut
shells using ethanol aqueous solution (60.5% v/v) as the solvent at
a temperature of 220 °C for a time period of 12.2 min. Under these
conditions, extracts with high phenolic yield like phenolic acids and
glycoside flavonoids were obtained.
Another study used pressurized liquid extraction method to
extract polyphenolic compounds with antioxidant activity from
Rubus fruticosus L. residues [66].
Anthocyanins were the main components recovered by using
water: ethanol (50 : 50) as extraction solvent in a dynamic extrac-
tion mode at 100 °C for a time period of 30 min.
Another example is the extraction of monomeric anthocyanins
and other phenolic compounds from grape (Vitis vinifera) pulp by
continuous liquid extraction [67]. The extraction was divided into
two consecutive parts to recover the different groups.
The first step was performed at 40 °C using water/ethanol
(50% w/w) pH 2.0 as solvent, and the second step was performed
at 100 °C using water/ethanol (50% w/w). The process yielded
two different sources: one rich in anthocyanins (first step) and one
rich in other phenolic compounds (second step). The low temper-
ature of the first step prevents thermal degradation of the antho-
cyanins before the second step, while the low pH aids the extraction
yield.
In the second step, efficient extraction of phenolic compounds
was found as high temperature increased the extraction of heat-
stable phenolic compounds.
Another interesting example is the recovery of biflavonoids and
anthocyanins from the dried fruit of Brazilian pepper (Schinus
terebinthifolius Raddi) after a defatting step in a continuous pres-
sure liquid extraction process [68]. The first step was to use petro-
leum ether at 60 °C for 6 min. In the second step, phenolic
compounds were extracted from the stone fruit and dried fruit
exocarp using acidified ethanol (5% v/v acetic acid) utilizing a static
Pressurized Liquid Extraction for the Isolation of Bioactive Compounds 287
extraction cycle (10 min each) at 75 °C and 100 °C. This continu-
ous supply of fluid facilitates the selective extraction of phenolic
compounds such as naringenin, biapigenin, and methylated
anthocyanins.
A combined application of pressurized liquid extraction and
ultrasonic-assisted extraction was used for the extraction of antho-
cyanins from Rubus fruticosus, Vaccinium myrtillus, and Eugenia
brasiliensis [69]. In this process, the sample is subjected to prelimi-
nary sonication before being extracted by pressurized liquid extrac-
tion. These samples were mixed by using hydroethanol solution
(50% or 70% ethanol) as menstruum and processed in an ultrasonic
bath at 80 °C for 8 min.
Pressurized liquid extraction is also used in biorefinery pro-
cesses to extract polyphenolic compounds. One study [70] carried
out the biorefining of hemp (Cannabis sativa L.) residues by
sequential supercritical carbon dioxide and pressurized liquid
extraction along with enzyme-assisted extraction. Lipophilic frac-
tion rich in cannabidiol and cannabidiolic acid was obtained in the
supercritical process, the pressurized liquid extraction method gave
a flavonoid-rich fraction, and the enzyme-assisted process gave a
sugar-rich fraction. The liquid extraction biotreatment process was
divided into two successive stages. In the first step, acetone was
used as the solvent and hydroethanol solution (4:1 v/v) was used in
the second step. Each step was performed at 100 °C for 45 min
(3 cycles × 15 min).
In another study [71], a continuous method was developed for
the isolation of bioactive compounds (human aromatase inhibitors)
from Cicer arietinum seeds using liquid extraction, countercurrent
chromatography, and preparative liquid chromatography.
The pressurized liquid extraction was performed using aqueous
ethanol (60% w/v) at 80 °C for 5 min. Thereafter, the extract was
transferred into the two chromatography sample loops. Both the
chromatography separations were optimized based on the polarity
of the active compounds already characterized in the pressurized
liquid extract.
The complementarity between countercurrent chromatogra-
phy and preparative liquid chromatography allowed the isolation
of 11 bioactive flavonoid-type compounds. This novel continuous
extraction method is effective and can be applied to other bioactive
compounds in various food or plants [72].
Recovery of phenolic compounds from various parts of medic-
inal plants has been made possible by pressurized liquid extraction.
The high temperatures and pressure and the right menstruum
bring about rapid and effective extraction of compounds of differ-
ent polarities [73].
Various fruits, vegetables, oils, such as Hibiscus sabdariffa caly-
ces, Sclerocarya birrea stem, pomegranate peel, sweet cherry stem,
and olive oil, have been subjected to pressurized fluid extraction to
288 Rakesh Barik et al.
5.8 Isolation of Pressurized liquid extraction technology has been used recently for
Terpenoids the extraction of terpenoid compounds from various sources
including plants and microorganisms [81]. Owing to the chemical
diversity and polarity, different solvents and temperature ranges are
required.
Pressurized Liquid Extraction for the Isolation of Bioactive Compounds 289
5.9 Extraction of The extraction of lipids is one of the principal uses of pressured
Lipids liquid extraction. This technique has been used to extract lipids
from a variety of sources and chemical structures utilizing low- or
medium-polarity solvents such as hexane, (+)-limonene, ethyl ace-
tate, methyl acetate, ethanol, and hydroethanolic combinations.
The temperature used for lipid extraction typically ranged from
90 to 220 °C. For the purpose of resolving issues with traditional
extraction techniques utilizing hazardous organic solvents, pressur-
ized liquid extraction was assessed as an environmentally friendly
method for isolating edible oils. For the effective extraction of
3-rich oil from Echium plantagineum seeds utilizing hexane-free
processing methods, pressured liquid extraction, microwave-
assisted extraction, and ultrasound-assisted extraction have recently
been examined [88].
Pressurized Liquid Extraction for the Isolation of Bioactive Compounds 291
5.10 Isolation of Pressurized liquid extraction has also been used to extract essential
Volatile Oils oils from plants. The most common method used for this applica-
tion is pressurized hot water extraction due to its high efficiency
and “green and clean” status for essential oil extraction. Due to the
large chemical composition of essential oils (terpenes, alcohols,
ethers, oxides, aldehydes, ketones, esters, amines, phenols, hetero-
cycles, etc.) in this technology, the temperature and cooling are
typically within 50–200 °C. The ability of this method to extract
essential oils has been analyzed and compared to hydrodistillation
and Soxhlet extraction methods [93].
In a study, pressurized hot water extraction method was used
with optimized conditions of temperature and flow rate for the
isolation of volatile oils from Matricaria chamomilla leaves. The
optimal conditions of temperature and flow rate (150 °C and
4 min mL-1 for 120 min) gave the best quality yield (14%) com-
prising of α-bisabolene oxides, β-trans-farnesene, and α-bisabolol
oxides A–B [94].
292 Rakesh Barik et al.
The same approach was used to obtain volatile oils from Cor-
iandrum sativum L. seeds [95]. The optimized conditions were
125 °C, 0.5-mm particle size, and 2.0 mL min-1 of water flow. The
extraction process showed an important volatile oils yield (14.1%);
however, hydrodistillation (21.7%) and Soxhlet (19.4%, using hex-
ane as solvent) methods presented the best performance. Neverthe-
less, it is worth mentioning that this technique obtains higher
quality volatile oils, since small amounts of hydrocarbons are
extracted. Another study used different extraction techniques
(hydrodistillation, Soxhlet, supercritical fluid extraction, and pres-
surized hot water extraction) to extract volatile oils from C. sativum
seeds [95]. In this case, supercritical fluid extraction (sc-CO2 at 40 °
C and 300 bar for 4 h) presented the best quality and yield;
however, under pressurized hot water extraction conditions
(200 °C for 20 min), it was possible to obtain an extract of volatile
oils rich in polyphenolic compounds with a higher added value.
Solvents other than water have also been explored for essential oil
extraction under pressurized liquid extraction conditions.
In a recent study, ethanol, ethyl acetate, and hexane were
evaluated for efficient extraction of α-bisabolol using pressurized
liquid extraction and ultrasonic extraction methods from the wood
of Eremanthus erythropappus.
α-Bisabolol is an important essential oil in many plants and is
used in skin preparations, cosmetics, fine perfumes, and shampoo
coatings. The highest purity content of α-bisabolol (64.23%) was
obtained under pressurized liquid extraction conditions (55 °C,
20 min extraction) [96].
7 Conclusion
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Abstract
Globally, fruits and vegetables generate almost half of total food waste, which has become a major
environmental concern. Though the ample amounts of fruit by-products are considered as industrial
waste and usually disposed of or used as animal feed and biofuel, they can be a great source of nutraceuticals
and bioactive compounds. Studies have suggested that bioactive compounds from fruit by-streams can be
extracted using conventional methods such as solvent extraction, maceration, and enzyme-assisted extrac-
tion and emerging technologies such as supercritical-fluid extraction, pressurized-liquid extraction,
microwave-assisted extraction, ultrasound-assisted extraction, and electric pulse field. This chapter discusses
the potential of extraction of nutraceuticals and bioactive compounds from fruit waste and their possibilities
for further application in the food, feed, cosmetic, and pharmaceutical industries, with their future
perspectives.
Key words Fruit waste, Valorization, Bioactive compounds, Nutraceuticals, Extraction methods
1 Introduction
Each year, more than 1.3 billion tons of edible food are wasted
globally, which is equivalent to nearly one-third of the entire
amount of food produced and more than enough to feed one
billion people. Less developed nations account for 44% of global
food waste during the post-harvest and processing stages of the
food supply chain, while developed nations in Europe, North
America, Oceania, Japan, South Korea, and China account for the
remaining 56% of these losses, of which 40% occur at the pre- and
postconsumer stages [1]. According to a United Nations report in
2017, the world population is estimated to reach 9.8 billion by
2050, and studies show that the world will need 70–100% more
food by that time. The only way to attain food security is by
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_13,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
299
300 Milan Dhakal et al.
minimizing food waste and food loss. Apart from food security,
food waste leads to monetary losses. Around the globe, the loss
from food waste accounts for $750 billion, which would directly
affect farmers’ and consumers’ incomes. The final disposal of food
waste in landfills (uncontrolled methane release) as well as the
production, processing, manufacture, transportation, storage, and
distribution of food all contribute to the emission of greenhouse
gases. Additional unfavorable externalities brought on by food loss
and waste include nutrient depletion, soil erosion, salinization, and
air and water pollution [2].
Fruit wastes, including citrus fruit skins, pineapple leftovers,
sugarcane bagasse, and other fruit residues (mostly peels and
seeds), are produced in enormous amounts in metropolitan areas
because of high consumption and industrial processing. One of the
main causes of municipal solid waste (MSW), which has become a
more challenging environmental issue, is fruit waste. Such wastes
are disposed of by landfilling or incineration. However, both tech-
niques impose various risks to the environment as well as human
health by releasing methane or secondary pollutants such as furans,
dioxins, and acid gases [3, 4]. In order to minimize those hazards,
recovering the bioactive components from fruit wastes, notably the
phenolic compounds, and fully utilizing them in food, pharmaceu-
ticals, and cosmetics seems to be crucial. Furthermore, value addi-
tion to agri-food waste is quite cost-effective and has minimal
impact on the environment [5]. Epidemiologically, consumption
of enough fruit and vegetables (10 servings or more per day) is
confirmed to prevent the inflammation and oxidative stress that are
linked to heart disease and diabetes, both of which have significant
mortality rates worldwide. The presence of secondary metabolites
such as fibers, carotenoids, anthocyanins, and phenols in fruits and
vegetables exhibit various antioxidant, anti-inflammatory, and
anticarcinogenic as well as biological activities [6–9]. These second-
ary metabolites are intended to help the plants grow and increase
their capacity for survival (resistance to environmental stress, ill-
nesses, and UV radiation). More than 15% of phenolic concentra-
tions are found in the skin of oranges, grapes, and lemons, as well as
the seeds of mangoes, avocados, and jackfruit than in fruit pulp.
However, a total of 55 million metric tons of biowaste are antici-
pated to be produced during each processing stage, including
5.5 million metric tons from the processing of fruits and vegetables,
6 million metric tons from canning and freezing, 5–9 million metric
tons from the processing of wine, and other sources. These losses
occur from different compositions such as under-ripe, over-ripe
fruits and vegetables or inedible parts including peels, rind, seeds,
core, rag, stones, pods, vine, shell, skin, pomace [10]. Along with
the fruit pomace, secondary metabolites such as fibers, carotenoids,
anthocyanins, and phenols are lost during manufacturing [11].
Fruit Waste: Potential Bio-Resource for Extraction of Nutraceuticals and. . . 301
2 Fruit Byproducts
Table 1
Summary of bioactive compounds in major fruit waste
(continued)
306 Milan Dhakal et al.
Table 1
(continued)
(continued)
Fruit Waste: Potential Bio-Resource for Extraction of Nutraceuticals and. . . 307
Table 1
(continued)
(continued)
308 Milan Dhakal et al.
Table 1
(continued)
(continued)
Fruit Waste: Potential Bio-Resource for Extraction of Nutraceuticals and. . . 309
Table 1
(continued)
3.2 Oils Fruit waste, especially seed/kernel parts, has a higher amount of
bioactive oil concentrated in it as compared to other parts. In the
research conducted by da Silva and Jorge [40] for different fruit
seeds, the lipid content ranged from 7.0% to 40.4%. Kernels/seeds
from different citrus fruits, apples, guava, tomato, grape, mango,
pumpkin, passion fruit, orange, melon, kumquat, etc. contain a
different proportion of fatty acids in their oil. These oils are poten-
tial sources of essential fatty acids. Major fatty acids in fruit oil are
palmitic acid (C16:0), palmitoleic acid (C16:1), stearic acid (C18:
0), oleic acid (C18:1), linoleic acid (C18:2), linolenic acid (C18:3),
and arachidic acid (C20:0). For example, in mango seed oil, steric
acid (C18:0) and oleic acid (C18:1) are the major fatty acids. While
in papaya, mango, and soursop seed oil, oleic acid (C18:1) and
linoleic acid (C18:2) are the major fatty acids. These oils are utilized
more frequently because of their greater health advantages in the
chemical, pharmaceutical, cosmetic, and food industries, as well as
for the direct development of functional foods. Fruit seeds and
their oils have added nutritional and health benefits due to phyto-
nutrients and phytochemicals, which are natural chemicals that take
part in a variety of biological processes, improve health status, or
prevent or treat sickness situations. Similar advantageous effects
have also been connected to other substances, including phenolics,
tocopherols, and carotenoids as well as lipids like FA, sterols, or
polar lipids. Fruit seed oils have been shown to have antioxidant,
antiproliferative, anti-inflammatory, and anti-diabetic properties.
Tocopherols act as primary antioxidants, as they donate one hydro-
gen atom to the peroxide radical, thus, interrupting the chain
oxidative process. There are 4 types of tocopherols mostly present
in fruit oil, namely: α-Tocopherol, γ -Tocopherol, β- Tocopherol,
and Δ-Tocopherol. α-Tocopherol is the most active homologous in
humans, and it performs the biological role of vitamin
E. Phytosterols and phytostanols present in fruit oil perform hypo-
cholesterolemic activity after ingestion by reducing cholesterol
absorption by the intestine.
3.3 Carotenoids Carotenoids are present in abundant amounts in both edible and
inedible portions of fruits and vegetables, but significantly higher in
inedible portions like peels and pomace. Different types of conven-
tional and novel green techniques are used to extract carotenoids
from fruit waste. Carotenoids in higher concentration have been
successfully extracted from many fruits wastes, that is, carrot bio-
waste (8.27 mg/100 g), mango pulp (2.18 mg/100 g), passion
Fruit Waste: Potential Bio-Resource for Extraction of Nutraceuticals and. . . 311
3.4 Vitamins Fruit waste is a rich source of several water-soluble vitamins, includ-
ing thiamine, niacin, riboflavin, vitamin C, and niacin, as well as
lipid-soluble vitamins, including vitamins A, D, E, K, and carote-
noids [42–44]. All three antioxidant vitamins A, C, and E can be
found in abundance in berries. Ascorbic acid can be found in a wide
variety of fresh fruits [45]. Vitamin C plays a crucial role in the
prevention of cancer because of its potent antioxidant action, which
shields our cells from oxidative damage. It is an effective electron
donor in biological systems in addition to possessing redox poten-
tial. Vitamin C lowers oxidative stress on the stomach’s mucosa,
DNA damage, and inflammation via scavenging reactive oxygen
species (ROS). By converting nitrous acid in the stomach to nitric
oxide and generating dehydroascorbic acid, it also prevents gastric
nitrosation and the creation of N-nitroso compounds. And finally,
it strengthens the host’s immune system. It inhibits stomach cell
growth and induces apoptosis, which directly affects the growth
and virulence of Helicobacter pylori [46]. The B-complex vitamins
(thiamine, riboflavin, and niacin) are crucial cofactors in biochemi-
cal processes and are necessary for healthy skin, normal body
growth and development, appropriate heart and neuron function,
and the production of red blood cells. Since individuals who suffer
from heart failure have a vitamin B deficit, vitamin Bs are directly
engaged in energy metabolism, and there is growing interest in
their potential to prevent heart failure [47]. Antioxidant-rich vita-
mins, such as lipid-soluble vitamins A, D, E, and K, can reduce the
risk of cardiovascular disease, cancer, and neurological disorders
[48]. Red and purple fruits have significant quantities of anthocya-
nins, which have bacteriostatic and bactericidal activity against
many pathogens (including Staphylococcus sp., Klebsiella sp., and
Helicobacter and Bacillus). Anthocyanins possess a variety of
biological effects, including anti-tumor, anti-inflammatory, antiox-
idant, anti-diabetic, and neuroprotective [49].
312 Milan Dhakal et al.
3.5 Alkaloids and Alkaloids and polyphenols are secondary metabolites of plants
Polyphenols which act directly by reducing activity, scavenging the free radical
and indirectly by chelating the prooxidant metal ions. Alkaloids are
water soluble compounds containing one or more nitrogen atom in
their molecule and possess significant biological activity. They
directly interact with neurotransmitters and results in various psy-
chological and physiological responses in human body [50]. Caf-
feine, theobromine, pipernine, quinine, capsaicin, solasodine,
solamargine, and solasonine are some examples of alkaloids com-
monly present in fruit waste [51]. Among all phenolics, dietary
phenolics, that is, polyphenols, flavonoids, and phenolic acids, are
considered to have major health benefits and preservative action in
food formulations. These compounds are rich in peel, rind, and
seeds of fruit waste. The major phenolic compounds present in fruit
seed oils are p-Coumaric acid, salicylic acid, and quercetin, with a
significant amount of gallic acid, catechin, caffeic acid, and epica-
techin in some fruits. Peels of citrus fruits contain bioactive com-
ponents and have been used traditionally in various places to treat
cough, muscle pain, digestive issues, and skin inflammation. Peels
of pomegranate contain punicagranine, an anti-inflammatory pyr-
rolizine alkaloid. Annona crassiflora fruit peels’ polyphenol-rich
fraction exhibits antioxidant properties that may find use in the
treatment of diabetes in clinical settings [52].
3.6 Bioactive These part of the fruit waste does not have a nutritional function as
Polysaccharides and they are resistant to enzymatic digestion in our body but has a vital
Dietary Fibers role in digestive function commonly known as cellulose and non-
cellulosic polysaccharides, that is, pectic substances, hemicellulose,
gums, mucilages, and other noncarbohydrate portions, such as
lignin, categorized as dietary fiber [53]. These compounds possess
several health benefits, such as regulating the feces output; reducing
the risk of obesity by providing a satiety effect, diabetics, and
hypertension; and lowering the occurrence of colorectal cancers
by trapping mutagenic substances and not allowing them to reach
the bloodstream [54].
3.7 Bioactive Protein The nonedible portion of fruits is a good source of bioactive
and Peptides proteins. For example, peels of citrus fruits ranged from 2.5% to
9.0% protein content [55, 56], whereas peels of papaya, kiwi, and
avocado fruit were found to be 1.55%, 1.79%, and 1.57%, respec-
tively [57]. Some enzymes have been discovered, which exert bio-
activity like actinidin from the seeds of kiwi fruit [58], vicilin-like
protein watermelons seeds [59], and leptin from seeds of jackfruit
[60]. Citrus natural peptides have been investigated as a potential
source of novel atheroprotective medicines due to their compara-
tive benefits over small molecules in the creation of anti-
inflammatory and cardioprotective drugs.
Fruit Waste: Potential Bio-Resource for Extraction of Nutraceuticals and. . . 313
3.8 Biogenic Amines The biogenic amines represent the nitrogenous compounds result-
ing from several enzymatic reactions, such as reductive amination,
decarboxylation, transamination, and degradation of the
corresponding precursor amino acids. Vasoactive amines, that is,
tryptamine, histamine, and tyramine have a positive role in blood
pressure control [61]. Five amines have been found in the study
conducted by [62] for pineapple, papaya, guava, mango, and pas-
sion fruit, that is, spermidine, putrescine, agmatine, serotonin, and
spermine. The total amine levels varied from 0.77 to 7.53 mg/
100 g in mango and passion fruits, respectively. Among these
amines, spermidine was detected in every test fruit sample, whereas
spermine and putrescine were detected in most of the samples.
Agmatine and serotonin were found in abundant amounts in pas-
sion fruits, papaya, and pineapple. Passion fruit seemed to be a
good source of polyamines spermine and spermidine, with 2.43
and 3.05 mg/100 g, which has an important role in maintaining
health, growth, and antioxidant activity and regulating membrane
permeability. Serotonin governs your mood and is responsible for
happiness. It also controls when you sleep and wake up, helps you
think, keeps your mood stable, and regulates your sexual drive. It is
also linked to the stomach to mediate reflex action and to lower the
risk of thrombosis.
Fig. 1 Schematic diagram of different extraction technologies for the extraction of bioactive compounds from
fruit waste
4.1.1 Soxhlet Extraction Soxhlet extraction has been used as a classical method of extracting
bioactive compounds from plant parts since ancient times. Though
the Soxhlet extraction method was designed for lipid extraction,
this method has been popularly used to extract bioactive com-
pounds from plants part including fruits. The advantages of Soxhlet
are it is simple and inexpensive. Nevertheless, this is time-
consuming and requires a large amount of solvents; thus, it is not
environmentally friendly. Alcohols, mostly ethanol and methanol,
Table 2
Extraction of bioactive compounds from different fruit waste using conventional and emerging technologies
Extraction
technique Fruit waste Bioactive compounds Extraction conditions Results References
C, 365 s
Grape cane byproducts Stilbenes 75 °C, ethanol (60%), [121]
10 min
315
(continued)
Table 2
316
(continued)
Extraction
technique Fruit waste Bioactive compounds Extraction conditions Results References
Supercitical Mango peel Flavonoids and carotenoids 30 MPa, 40 °C, carbon [122]
fluid dioxide flow rate
extraction 1.1 L/min, 7.7 h
(SFE)
Milan Dhakal et al.
Pulse electric Grape byproducts Anthocyanins 3 kV/cm 2 folds higher than [123]
field (PEF) control
Mango peel Mangiferin, quercetin, ellagic acid 13.3 kW/cm, 60 °C, Extracted with high [124]
1000 kJ/kg clarity and
colloidal stability
Enzyme- Guava leaves Phenolics Cellulase or beta- Yield increased by [125]
assisted glucosidase-assisted 103.2%
extraction extraction
(EAE) Pistachio green hull Phenolic compounds Cellulase, pectinase and Yield increased by [126]
tannase, pH 4.0, 37 °C 112%
Pressurized Pomegranate peel Phenolic compounds 3 MPa, 126.1 °C, solvent- [127]
liquid solid ratio 54.8 mL/g,
extraction 18.5 min
(PLE)
Fruit Waste: Potential Bio-Resource for Extraction of Nutraceuticals and. . . 317
4.1.2 Hydro-distillation Several bioactive compounds including oils are extracted using
hydro-distillation technique. Water and steam distillation, water
distillation, and direct steam distillation are three different types
of hydro-distillation methods. In this extraction technique, the
sample is completely immersed in boiling water. This process
undergoes different physicochemical processes such as hydro-
diffusion, hydrolysis, and thermal decomposition. However, this
technique is not appropriate for heat-sensitive compounds as they
might be lost or degraded during the extraction process. The
advantages of this extraction technique are: no use of organic
solvents and shorter extraction time.
4.2.3 Supercritical Fluid Supercritical fluid is a hybrid media that possesses combined prop-
Extraction erties of liquid and gases in a single phase. Supercritical fluid extrac-
tion (SFE) does not require toxic organic solvent; hence, it is
considered a green technology. The advantage of using supercritical
fluids for recovery of bioactive compounds from fruit waste is that
supercritical fluid has low viscosity and high coefficient of diffusion
as compared to conventionally used liquid solvents. These proper-
ties promote efficient extraction of bioactive compounds by allow-
ing the fluid to penetrate into the matrix to a greater extent. Fluids
such as carbon dioxide, water, methanol, ethylene, ethanol,
n-butane, and n-pentane at pressure and temperature above their
critical points are used in SFE. The most used fluid in supercritical
fluid extraction is carbon dioxide as it is relatively inexpensive,
nonpolar in nature, nontoxic, and nonflammable. The low polarity
of carbon dioxide enhances the extraction of nonpolar or small
polar biomolecules such as lipid and volatile compounds
[152]. However, supercritical fluid extraction with carbon dioxide
could efficiently extract nonpolar or mid-polar compounds (essen-
tial oils and carotenoids). The yield and purity of extracted bioactive
compounds from fruit waste depend on several factors, such as
temperature, pressure duration, solvent flow rate, amount of
co-solvent used, co-solvent flow rate, the nature of fruit waste,
and prior processing technique (drying, lyophilization, etc.). Avail-
able literature suggests that supercritical fluid extraction has advan-
tage over conventional extraction in terms of selectivity, compound
stability, easy recovery, and time and energy saving. Pham [122]
322 Milan Dhakal et al.
4.2.4 Pulse Electric Field Pulse electric field extraction technology is an energy-efficient and
Extraction environmentally friendly process that uses high voltage pulses of
electricity, which is used in food processing to prolong shelf-life.
However, it has been equally used for the extraction of bioactive
compounds. In PEF treatment, the food sample is subjected to
electrical resistance of 20–80 kV/cm for very short time (<1 s) to
produce high energy discharges. When the electric pulse is applied
to plant tissue, it increases tissue softness through electroporation
of cell membranes. Electroporation depends on energy, time, and
number of pulses. The pore size and wall/membrane disintegration
increase with the intensity of electric pulses; the main factor in play
to govern optimization of PEF extraction is electric field/mass ratio
[144, 153–155]. Studies have suggested that use of PEF for bioac-
tive compound extraction improves the extraction yield. Corrales,
Toepfl [123] reported that the use of PEF to extract anthocyanins
from grape byproducts enhanced the yield of anthocyanins, and
PEF could also be used to selectively extract targeted bioactive
compounds. Moreover, the extraction depends on pH, extraction
time, electric field strength, pulse shape, pulse width, pulse fre-
quency, food matrix density, and the chemical properties of the
compound to be extracted. Parniakov, Barba [124] reported that
application of pulse electric field–assisted extraction significantly
increased the extraction yield of polyphenol (mangiferin, quercetin,
ellagic acid) from mango peel. Moreover, Delsart, Ghidossi [156]
extracted anthocyanins and polyphenols from grape skin using PEF
and observed that the extraction yield of these compounds was
higher than other extraction techniques. Plum and grape peels
[157], orange [158] and lemon [159] peel residues, or olive pom-
ace [160] are additional examples of byproduct valorization by
PEF-assisted polyphenol extraction. PEF has several advantages
over conventional extraction technology, which include: (a) no
water removal or dehydration of samples, (b) additional chemicals
not needed, (c) no heating needed, (d) less time-consuming,
(e) scalability. However, more research is still needed on the effects
of pulsed electric fields on pulsed matrices.
Fruit Waste: Potential Bio-Resource for Extraction of Nutraceuticals and. . . 323
4.2.5 Enzyme-Assisted Enzymes are also used to extract bioactive compounds from food
Extraction waste including fruit waste. Enzymes such as cellulase, pectinase,
hemicellulase, xylanase, β-gluconsae, β-glucosidase, and alcalase can
decompose the cell wall materials (pectin, hemicellulose, and cellu-
lose) of fruit waste and can assist in the extraction of bioactive
compounds [161]. Since EAE utilizes water as solvent rather than
organic solvents, it is considered as the most ecologically friendly
extraction technique. Factors that should be considered during
enzyme-assisted extraction are type and concentration of enzyme,
extraction temperature, particle size, water-to-solid ratio, time, and
pH. More specifically, pH and temperature are critical to activate
catalytic potential. Further, the efficiency of enzyme-assisted extrac-
tion could be maximized when assisted with other processes such as
ultrasound, microwave, and so on. Wang, Wu [125] treated guava
leaves with cellulase or beta-glucosidase-assisted extraction and
found that the extraction of phenolics increased by 103.2%.
Enzyme-assisted extraction is gaining popularity in the valorization
of polyphenol-rich matrices from food-agroindustry since it is an
environmentally friendly approach [162]. Similarly, Ghandahari
Yazdi, Barzegar [126] used the combination of different enzymes,
cellulase, pectinase, and tannase, at optimal conditions (pH 4.0,
37 °C) to extract phenolic compounds from pistachio green hull
and compared to the conventional control extract. They observed
that the yield of phenolic compounds increased by 112%, and the
antioxidant capacity was found to be 71% higher than extract
without enzyme treatment [126, 163]. Treatment with cellulase
and tannase to recover polyphenols from Syrah grape pomace
increased the recovery of phenolics (up to 66%) as well as the
antioxidant activity (up to 80%), compared to classic hydroalcoholic
(50:50) extraction at 50 °C for 6 h [163, 164].
4.2.6 Pressurized Liquid Pressurized liquid extraction (PLE), also known as accelerated
Extraction solvent extraction (ASE), was introduced as an extraction technol-
ogy by Dionex Corporation for the extraction of anthocyanin from
seaweed [139]. PLE is also a green extraction technology that uses
water instead of organic solvent and reduces the amount of solvent
used to extract bioactive compounds from fruit waste. The pressur-
ized liquid extraction technique employs pressure (between 5 and
15 MPa) to keep the solvent at a temperature higher than its boiling
point. PLE, solid-liquid extraction technique, uses pressurized sol-
vents at high temperature (>100 °C). The high temperature and
pressure applied increases the solubility and mass transfer rate of
bioactive compounds. The high pressure used aids the penetration
of the solvent into the pores of the solid material and the high
temperature facilitates diffusion of the solvent into the solid mate-
rial. PLE has been frequently applied for the extraction of phenolic
compounds, carotenoids, and tocopherols from fruit waste. Xi, He
[127] have extracted phenolic compounds from pomegranate peel
324 Milan Dhakal et al.
with PLE at 3 MPa, 126.1 °C, solvent-solid ratio 54.8 mL/g, and
extraction time of 18.5 min. The extraction of bioactive com-
pounds using pressurized liquid extraction technique is the func-
tion of factors such as solvent polarity, toxicity of solvent, particle
size, mass transfer rate, sample moisture content, temperature,
pressure, and extraction time.
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Chapter 14
Abstract
The greatest difficulty facing the cosmos now is the ability to survive in excellent health. The idea that
nature preserves plant seeds when they are dormant and have been sitting in the soil for a long time is the
foundation for the current notion. Bacteria, fungus, and virus attack are deterred from attacking seeds with
the assistance of antimicrobial phytochemicals, plant defensins, other associated antimicrobial biopeptide
components, plant prebiotics, probiotics, postbiotics, etc., prepared by the seeds during its journey towards
the matured plant. Nature uses this technique to safeguard the offspring. We merely need to understand
what nature is trying to tell us. The aim of the chapter is to take us through this message of nature followed
for the well-being and growth of plant life cycle. Readers shall be acquainted with the current state of
knowledge on plant seeds as a potential bioresource for the extraction of nutraceutical and bioactive
chemicals. Moreover, the chapter will take the reader through Mother Nature’s ways of green extraction
techniques like sprouting, germination, and fermentation for the health benefits of human beings.
Key words Plant seeds, Antimicrobial biopeptide, Prebiotics, Probiotics, Postbiotics, Green extrac-
tion, Sprouting, Germination, Fermentation
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_14,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
333
334 Gitanjali Sambhajirao Deokar et al.
bioactive resources from the plants seeds. Further, how these bio-
active compounds involved in defense and healthy growth of plant,
which could be beneficially utilized for commercial exploitation of
the products for human health benefits.
1.2 Concept Behind Seeds are a crucial component of the ecosystem process because
Plant Seed Survival they enable plants to adapt to changing environments, maintain
and Longevity existing populations, and establish new populations in suitable areas
through a scatter network. Thus, seeds play a variety of significant
roles in the physiology, ecology, and geography of plants [20].
Two key factors, seed lifetime and seed dormancy, are used to
control seed quality. The most important quality of the seed is its
resistance to deterioration. Seed dormancy, which limits seed ger-
mination under unfavorable conditions and prevents the plant from
concluding its life cycle without losing its ability to grow in the
appropriate conditions, serves as the plant’s protective mechanism.
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 337
2.1.1 Defensins Plant defensins are the vast antimicrobial peptide superfamily found
across the plant world [27]. Plant defensins are small, highly stable,
rich in arginine, lysine, and cysteine residues, that constitute a part
of the innate immune system. These are large family of cationic
host defense peptides (HDP) [30]. The first plant defensins were
isolated from wheat Triticum aestivum L and barley Hordeum
vulgare and initially classified as gamma thionins. Plant defensins
are small basic, cysteine-rich peptides ranging from 45 to 54 amino
acids with low molecular weight about 5 kDa. Biological activities
reported for plant defensins include antifungal, antibacterial, pro-
teinase, and insect amylase inhibitor activities [28]. Additionally, it
has been reported that these compounds mediate abiotic stress and
zinc tolerance, inhibit protein synthesis, impair ion channel func-
tion, and hinder microbial, root hair, and parasitic plant growth,
change the redox state of ascorbic acid, stimulate the perception of
sweetness, act as epigenetic factors, influence self-incompatibility,
and support male reproductive development [31]. Plant defensin
genes produce precursor proteins that target a signal at the amino
terminal and a pro-peptide at the c-terminal (CTPP) and have a
mature defensin domain.
This CTPP is optional; some defensins may contain it while
others do not. Class II plant defensins are defined as peptides with a
c-terminal pro-peptide signal (CTPP) of 27–33 amino acid resi-
dues. Glutamic and aspartic acids, which have a negative charge and
balance the positive charge of the defensin domain, are prevalent in
these amino acid residues. Class I is assigned to the other class that
is deficient in these signals. Class I plant defensins are only detected
in the seeds, but class II plant defensins are reported to be abun-
dantly produced in both the reproductive and vegetative sections of
the plant [32–34].
Activation Process of The study projects carried out by the co-researcher Terras F et al. in
Defensins in Seeds 1995 provided illuminating insight into the activation mechanism
of defensins for the execution of their functional tasks. Raphanus
sativus-antifungal protein-1 (RsAFPl) and Protein-2 (RsAFP2),
two homologous, 5-kD cysteine-rich proteins found in radish
seeds, both demonstrate strong antifungal action in vitro. In their
340 Gitanjali Sambhajirao Deokar et al.
Table 1
Representative examples of plant seed antimicrobial peptides (AMPs) isolated using germination
process and their classification and bioactivities
Sr.
no. Plant seed AMP Peptide Function Reference
1. Radish seeds Defensins 5-kD cysteine-rich Antifungal activity [35]
[Raphanus proteins, Raphanus against foliar
sativus] sativus-antifungal pathogen Alternaria
protein-1 (RsAFPl), longipes
and Protein-
2 (RsAFP2)
2. Lentil seeds [Lens Defensins Lentil seed defensin Activity against [96]
culinaris] termed as Lc-def has Aspergillus niger
8 cysteines forming (Aspergillus niger
four disulfide bonds. causes sooty mold on
A 74-residue onions and
predefensin contains ornamental plants)
a putative signal
peptide (27 amino
acid) and a mature
protein
3. Pearl millets, Thionins Thionins (PR protein- Sporangia. graminicola [39]
[Pennisetum 13) are a class of zoospores lysis
glaucum (L.) Cys-rich polypeptides
R. Br.] of about 5 kDa
cultivars
IP18292
4. Black cumin Thionins Nigellothionins- Growth inhibitory [97]
seeds [Nigella dominant peptide, activity against
sativa (L.)] NsW2 with 8-Cys filamentous fungi
motifs and yeasts
5. Rice seeds [Oryza Lipid transfer OsLTPL36, a homolog Seed quality seed [45]
sativa] proteins of putative lipid development and
transport protein seed germination
6. Castor bean Lipid transfer Nonspecific lipid Regulation of fatty acid [98]
[(Ricinus proteins transfer protein, β oxidation through
communis (nsLTP) enhancement of
(L.)] acetyl CoA oxidase
activity in
glycosomes (nsLTP
as acetyl CoA carrier-
energy source and
helps in cellular
respiration
(continued)
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 341
Table 1
(continued)
Sr.
no. Plant seed AMP Peptide Function Reference
7. Lentil seeds [Lens Lipid transfer Lc-LTP 1–8, (92–93) Antibacterial: Inhibit [99]
culinaris] proteins amino acid residues, growth of
with four disulfide Agrobacterium
bonds tumefaciens.
(causative agent of
crown gall disease)
8. Sweet violet Cyclotides Peptides with cyclic, Act as defense and [47]
seeds [Viola cystine knot storage proteins
odorata] structural motif
9. Alfalfa seed Snakins MsSN1 has a putative Antibacterial and [51]
[(Medicago signal peptide of antifungal activity,
sativa (L.)] 25 amino acids and helps in plant innate
possesses a snakin/ immunity
GASA domain
(Pfam02704)
containing
12 cysteine residues
in conserved
positions within a
conserved C-terminal
region
10. Quinoa seeds Hevein-like Type III lectin Inhibition of [55]
[Chenopodium proteins precursor, CB-HLPs phytopathogenic
quinoa] (chitin-binding fungi
hevein-like peptides –
cysteine-rich
peptides) chenotides,
tandem repeats of the
mature peptide
domains, with a
cleavable Gly/Ala-
rich linker consisting
of 18 amino acids
research, it was shown that these proteins are found in the cell wall
and are more common in the lining of the outer cell layers of several
seed organs. Additionally, following breakdown of the seed coat,
RsAFPs are selectively released during seed germination. The num-
ber of proteins produced is sufficient to provide a microenviron-
ment that inhibits fungal development surrounding the seed
[35]. There is also documented additional material that supports
the idea that external stimuli activate defense mechanisms. It was
discovered that when a vegetative plant tissue is injured or detects
342 Gitanjali Sambhajirao Deokar et al.
2.1.2 Thionins Thionins are a family of antimicrobial peptides that are found in the
seeds, stems, roots, and leaves of cruciferous plants, mistletoe, and
cereals. They have a low molecular weight (approximately 5 kDa)
and are highly concentrated in arginine, lysine, and cysteine resi-
dues. Thionins are poisonous to yeast, fungus, and bacteria. It was
proposed that their activity resulted from the lysis of the mem-
branes of adhering cells. Antifungal activity shown by thionins, is
a result of electrostatic interactions between positively charged
thionins and negatively charged phospholipids in fungal mem-
branes, which lead to the creation of pores or a particular contact
with a particular lipid domain [28]. The typical 5 kDa, basic thionin
peptide with three or four disulfide bridges is obtained by first
producing them as preproproteins and then processing them. Tran-
scriptomes of more than 1000 plant species have been sequenced as
part of the “one thousand plant transcriptomes initiative” (1KP
project). New thionin sequences were sought using the data. The
four types of thionins that were previously identified, only two
classes and their variants are presently recognized using the data
from the 1KP study. Due to the fact that every variant was linked to
either class 1 (eight cysteines) or class 2 (six cysteines). Eighteen
versions in total were found by the 1KP project with all the distinct
variants [38].
2.1.3 Lipid Transfer Nonspecific lipid transfer proteins(LTPs) are small, cysteine-rich
Proteins proteins that have a variety of functional roles in the growth and
development of plants, including the production of cutin wax,
adhesion of pollen tubes, cell expansion, seed development, germi-
nation, and adaptation to changing environmental conditions.
LTPs have a hydrophobic cavity with eight conserved cysteine
residues that allows for a wide range of lipid-binding specificities.
Many LTPs serve as positive regulators of plant disease resistance
because they are members of the pathogenesis-related protein
14 family (PR14) [43]. Researchers are interested in LTPs for
three basic reasons. Plant LTPs have two distinct properties. First,
they can bind and transfer lipids, which is how they received their
names and were grouped into one class. The second characteristic is
that LTPs are protective proteins that are part of innate plant
immunity. The third characteristic is that one of the most therapeu-
tically significant classes of plant allergens is represented by
LTPs [44].
Activation Process of Lipid In the studies reported in 2015 by Wang et al., a homolog of a
Transfer Proteins in Seeds putative lipid transport protein was revealed to exhibit unique
expression in the developing rice seeds. Homolog was predomi-
nantly expressed in developing seed coat and endosperm aleurone
344 Gitanjali Sambhajirao Deokar et al.
2.1.4 Cyclotides A cystine knot made up of three disulfide bonds stabilizes the
globular microproteins known as cyclotides, which have a distinc-
tive head-to-tail cyclized backbone. Compared to other peptides of
comparable size, they exhibit excellent stability to chemical, ther-
mal, and biological degradation because of their distinctive circular
backbone topology and knotted arrangement of three disulfide
links. Multiple cyclotides (between 10 and 160) are typically pres-
ent in every tissue of a single plant, including the flowers, leaves,
stems, roots, and perhaps even the seeds [46].
Activation Process of Slazak, B., et al. (2020) described experiments involving variations
Cyclotides in Seeds in the quantity of cyclotides in developing seeds of Viola odorata.
To soften the seed coating, sterilized seeds were placed in a beaker
with wet paper and kept at 4 °C for 7 days. The seed coating was
then taken off, and the seeds were placed on half-strength MS
media that had been thickened with 7 g/l agar. Three distinct
stages of seedling development—the seed, a germinated seedling
with endosperm, and seedlings that utilized the entire
endosperm—were collected and freeze-dried after seeds were
grown in a culture chamber. The growing seedling appeared to
ingest cyclotides found in the seed endosperm. It was found that
the cyclotide pattern found in various tissues and surroundings is
shaped by degrading processes. The findings show that various
cyclotides have distinct functions, some of which are related to
defense and others which are related to storage proteins [47].
2.1.5 Snakins Snakins are typically tiny, positively charged, cysteine-rich proteins
with a molecular weight of about 7 kDa that play a number of roles
in plant defense responses, including antimicrobial action against a
wide variety of phytopathogens and animal diseases. Snakin-1
(StSN1), the first recognized Snakin peptide, was isolated from
potato tubers and given the name Snakin because it had sequence
features with snake venoms. The 12 cysteine residues that are
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 345
Activation Process of Understanding the activation and use of Snakin peptides for anti-
Snakins in Seeds fungal action in alfalfa seeds was made possible by Garcia et al.
(2014). Sterilized seeds of both transgenic and wild types were
put in petri dishes with 1% agar water under 16 h of light
(100 moles/m2s) and 25 °C.
Plants were moved to 1:1 vermiculite: perlite and kept
in magenta vessels to preserve humidity after being incubated at
25 °C with a 16 h photoperiod for a month. Phoma medicaginis was
sprayed onto all aerial tissues of two-month-old plants to inoculate
them. The percentage of sick leaflets was examined 30 days after
vaccination, and 60 days later, the number of regrowing plants and
the percentage of heavily defoliated plants were counted. Snakin-1
produced by alfalfa (MsSN1)-overexpressing alfalfa transgenic
plants exhibits increased antimicrobial activity against virulent fun-
gal strains without changing the nitrogen-fixing symbiosis, paving
the way for the development of efficient alfalfa transgenic cultivars
for biotic stress resistance [51].
Activation Process of Another work by Shining Loo 2021, examined the hyperstable
Hevein-Like Proteins in antifungal Chitin-binding hevein-like peptides (CB-HLPs) cheno-
Seeds tides found in quinoa seeds (Chenopodium quinoa). The biosynthe-
sis of chenotides was shown to be novel and to belong to a new
family of cleavable hololectins, which were designated as type III
lectin precursors. These precursors were tandem repeats of the
mature peptide domains with an 18-amino-acid cleavable linker
between them. Chenotides can also stop the growth of phyto-
pathogenic fungi because they link to chitin. It has been noted
that the presence of chenotides, which are naturally occurring
anti-microbial agents, in quinoa may be the underlying cause of
the grain’s prolonged shelf life and unintentional selection as a
staple food throughout human history [55].
3.1 Endophytes of The genetic spread of endophytes across generations of hosts can
Seeds occur via seeds. Seed endophytes are founders of the juvenile plant
microbiome and can aid host defense during seed germination and
later phases. Endophytes are symbionts that live inside plant tissues,
including seeds. The findings were reported by Khalal and Raizada
2018, by using dual culture assay methodology wherein they exam-
ined the in-vitro antagonistic effects of endophytes from seeds of
various cultivated cucurbits against significant soil-borne pathogens
like Pythium aphani dermatum, Phytophthora capsici, Fusarium
graminarium, and Rhizoctonia solani. For the purpose of inducing
plant defense, the endophytes were also examined in-vitro for their
ability to secrete volatile organic compounds. It was discovered that
fungal infections were suppressed when extracellular ribonuclease
activity was also examined. These findings demonstrate that the
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 347
Table 2
Representative examples of plant seed germination/sprouting for isolation of endophytes, epiphytes,
amino acids, enzymes, probiotics, prebiotics, with their classification and bioactivities
Sr.
no. Plant seed Bioactive component Function Reference
1. Fruits and seeds- Endophytes: Lactococcus, Anti-oomycete activity [56, 100]
Cucurbitaceae family Pantoea, Pediococcus
(examples: melon
(Cucumis melo),
cucumber (Cucumis
sativus)
Water melon (Citrullus Activity against
lanatus) t Podosphaera fuliginea
responsible for powdery
mildew on cucurbits
Squash and pumpkin Diverse nutrient
(Cucurbita sp.) acquisition and growth
promotion activities to
the hosts
Seeds belonging to Phyla These microbes may lead to
(Firmicutes, novel seed inoculants to
Proteobacteria) and one assist sustainable food
class within each phyla production
(Bacilli, γ-proteobacteria,
respectively)
2. The asymptomatic wheat Endophytes: Dominant Growth and disease [101]
[Triticum aestivum (L.) bacterial genus identified resistance of wheat plants
cv.] Heixiaomai NO.76) are Erwinia and (antibacterial and
seeds (sterilized sprouted Rhizobiales) and antifungal)
seeds) dominant fungal genus
identified is Emericella
3. Seeds of Brassica (B. juncea Epiphytes: Total epiphytic Antimicrobial biocontrol [102]
L. Czern., B. rapa L., microbial load of 106– agent
B. napus L.) and Triticum 108 bacterial genomes g-
1
(T. aestivum L., seeds was observed.
T. turgidum L. subsp. Examples: Pantoea
durum (Desf.) Husn.) agglomerans
4. Soybean (Glycine max), Enzymes proteases A protease is an enzyme that [74]
Lentil (Lens esculenta), catalyzes proteolysis,
Black gram (Vigna breaking down proteins
mungo), Green gram, into smaller polypeptides
(Vigna radiata) Bengal or single amino acids, and
gram, (Cicer arietinum) spurring the formation of
Groundnut (Arachis new protein products
hypogaea), Pea bean
(Phaseolus vulgaris)
(continued)
350 Gitanjali Sambhajirao Deokar et al.
Table 2
(continued)
Sr.
no. Plant seed Bioactive component Function Reference
5. Sword bean seeds Enzyme α-amylase α-Amylase is an enzyme that [103]
(Canavalia gladiata hydrolyses α bonds of
(Jacq.) DC.) large, α-linked
polysaccharides, such as
starch and glycogen,
yielding shorter chains
thereof
6. Germinating oil seeds Enzyme lipase Lipases are versatile enzyme [104]
(Brassica napus L.) that catalyzes the
hydrolysis of ester
linkages, primarily in
neutral lipids such as
triglycerides
7. Pigeon pea seeds Amino acids Nutritional quality and [105]
(Cajanus cajan) bioactivity of seeds
increases. Germination
helps in increase in
essential and non-
essential amino acids,
digestibility of crude
proteins increases by
conversion to amino
acids
8. Lentils (Lens culinaris), Probiotics: Lactobacillus Beneficial effects on human [61]
Mung beans, (Vigna and Bifidobacterium physiology
radiata), Peanut
(Arachis hypogeal)
9. Faba bean (Vicia faba L.), Prebiotics Serves as food for gut flora, [106]
Lentil (Lens culinaris), Raffinose family undergo anerobic
Common bean (Phaseolus oligosaccharides fermentation in large
vulgaris), and Cowpea account for 67.3, 63.2, intestine
(Vigna sinensis) 53.0, and 51.0% of the
total soluble sugars in
cowpea, faba bean,
lentil, and common
bean, respectively
Other oligosacchrides like
Verbascose in faba bean
and stachyose in the
other three legumes
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 351
4.1 Germination vs. Germination is the process by which a seed transforms into a new
Sprouting plant after achieving the conditions necessary to end its dormant
state. The only seeds that germinate are those that have an embryo
in them. The process of germination causes a seed to grow into a
seedling, which subsequently forms the plumule and radicle. The
post-germinative growth of the seedling is thought to occur after
seed germination, which is regarded as the beginning of the first
developmental phase in the life cycle of higher plants. When the
environment is right, a seed will begin to germinate in response to
factors like light, temperature, soil elements and well-understood
chemical pathways. The mature seed resumes growth during the
intricate process of germination, switching from a maturation- to
germination-driven programme of development and subsequent
seedling growth. By definition, a seed’s germination process begins
with the absorption of water and is finished when the radicle
emerges from the surrounding structures [64].
When a monocotyledonous plant seed germinates, the coleo-
rhiza is the first component to emerge from the seed coat, however
when a dicotyledonous plant seed does the same, the radicle
emerges first. The pace at which seeds are absorbing water deter-
mines how quickly they are germinating in both groups. Phase I of
the process begins with a dry seed rapidly absorbing water until all
of the seed tissues are saturated. Phase II is then followed by a
modest intake of water, but phase III is followed by a significant
uptake of water that is associated to the completion of germination.
Phase II is the most significant and is connected to a number of
cellular and physiological processes, including DNA repair and the
translation of both newly generated and stored mRNAs. Both
enhanced metabolic and cellular activity define Phase II. In order
to generate seedlings, embryo cells must decide whether to re-enter
the cell cycle or remain arrested during the germination stage.
When a seed germinates, the quiescent seed’s stalled cell cycle is
released [64].
Understanding the notion of germination of the particular seed
will help you extract functional and neutraceuticals components
from the seeds while taking the same procedure emulating natural
seed germination process into consideration. By optimizing the
many factors related to the process completion, components
could be activated, extracted, and isolated. Sprouting may be
viewed as a commercial green extraction method that could be
optimized for component isolation.
“Sprouts” (Regulation (EC) No 208/2013) are “the product
obtained from the germination of seeds and their development in
water or another medium, harvested before the development of
true leaves and which is intended to be eaten whole, including the
seed” [65, 66].
352 Gitanjali Sambhajirao Deokar et al.
4.1.1 Understanding the Understanding the natural germination process of seed is required
Germination Process to for the optimization of sprouting for commercial use. Most agri-
Optimize Extraction by cultural seeds need water, a suitable temperature, and a good
Sprouting Process gaseous atmosphere for germination. Dormancy is a significant
element in the emergence of weeds but has minimal effect on the
seedling emergence of the majority of commercial crops. Addi-
tional germination-promoting elements for weed seeds to consider
are sunshine and nitrate [68]. Let us have a look at various factors
impacting the germination/sprouting process.
Effect of Water Uptake/ Three phases of water intake by the seed are typically observed: a
Imbibition rapid initial phase, a lag phase with little additional uptake, and
finally a second phase of rapid water uptake linked to radicle emer-
gence. Although metabolism begins before seeds achieve their
maximum moisture content, imbibition is recognized as a physical
process and is associated with the first stage of water uptake. Initial
water intake is propelled by matric pressures brought on by the
hydration of protein and starch bodies, cell walls, and other cellular
components. There is an increasing dependence on osmotic poten-
tial, which is defined by the concentration of dissolved solutes, as
the physiological range of water levels is approached. The viability
of seeds and the success of seedling emergence can both be signifi-
cantly harmed by the rate of early water intake. Rapid ingestion can
harm both directly and indirectly through a favorable interaction
with chilling injury. The quality of the seed coat and other factors of
seed vigor directly influence how much harm has been done. By
modulating permeability, the seed coat and other tissues can also
play a significant regulatory role in water intake. Germination is
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 353
Effect of Temperature and Temperature and water potential together have a significant impact
Water Potential Threshold on the percentage of seeds that will germinate, germination time,
and spread of timings within the seed population.
(a) Temperature: Although seeds can sprout at a variety of tem-
peratures, the maximum percentage of germination is often
reduced at the extremes of the temperature range. Because of
this, various seeds within a population may have varied thresh-
olds for high and low temperatures. Germination rate, which
is the reciprocal of germination time for each individual seed in
the population, rises from a base temperature to an ideal
temperature, after which it declines to a ceiling temperature
that represents the upper limit of its tolerance [68].
(b) Water: It has been demonstrated that the pace of development
toward 50% germination is linearly proportional to water
potential, much like with temperature. A scale similar to ther-
mal time called hydro time can be used to describe how seeds
react to various water potentials [68].
Effect of Oxygen on One of the limiting elements in seed germination is oxygen since
Germination germination necessitates the metabolism of storage chemicals,
which depends on respiration. Oleg A. Kuznetsov and
K.H. Hasenstein studied the germination of flax seeds in relation
to oxygen requirements in their 2003 investigations. In trials with
controlled atmospheres, as the oxygen concentration in the atmo-
sphere was dropped, the length of roots and percentage of germi-
nation fell. Seeds absorbed water but did not germinate after 2 days
in environments with less than 5% oxygen. At 10% oxygen, germi-
nation was nearly as high as that of the controls (21% O2), however
the root length was decreased to less than 50%. The seeds grew
when the temperature was 27 °C, which is ideal for the growth of
flax seedlings.
At constant temperature, the root length grows linearly. A
steady oxygen supply and an even number of seeds per chamber
affected the germination rate, demonstrating the importance of
oxygen for the best possible seed germination [69, 70].
Effect of Light on Effect of light on seed germination and seedling form of succulent
Germination species from Mexico were both shown in studies by Joel Flores et al.
in 2015. According to previous research, the adult plant height and
354 Gitanjali Sambhajirao Deokar et al.
4.1.2 Extraction by The study highlights of Kamala Golla and coresearchers 2016 are
Sprouting considered here for representing isolation of antimicrobial peptides
using sprouting technique. The presence of short peptides with
Sprouting for Isolation of antimicrobial peptides was extensively examined in 50 distinct
Antimicrobial Peptides types of germinating seeds. Proteins were extracted using both
liquid nitrogen and phosphate buffer (PBS) treatments after
selected seeds were germinated on brown sheets over a period of
time. Small peptides of less than 10 kDa were formed by 5 kDa flow
through, and the same was validated by SDS-PAGE (sodium dode-
cyl sulfate–polyacrylamide gel electrophoresis). Staphylococcus
aureus, Escherichia coli, Klebsiella pneumoniae, and Pseudomonas
aeruginosa were the four clinical isolates against which the short
peptides that had been extracted were tested for antibacterial effi-
cacy. Staphylococcus aureus (MTCC 9542), Escherichia coli (MTCC
1698), Klebsiella pneumoniae (MTCC 10309), and Pseudomonas
aeruginosa (MTCC6458) were the reference/standard organisms
employed in this investigation. All cultures were subcultured on
nutrient agar at regular intervals and preserved at -20 °C and 4 °C,
respectively, by suspending them in 10% glycerol. Using 1% mercu-
ric chloride, the surfaces of jowar, paddy, millets, foxtail millets, red
gram, green gram, black gram, ground nut, pea, field bean, and
wheat seeds were sterilized. Depending on the seed variety, the
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 355
seeds were soaked in distilled water for 6–12 h before being placed
on sterile brown paper and allowed to germinate for 2, 4, 6, 8,
10, 12, 14, or 16 days, respectively, at 26 °C. A 10% moisture
reduction was achieved by drying ungerminated and germinated
seeds at 600 °C. Before usage, these samples were stored in tightly
packed polyethylene bags at 40 °C. Using a pre-chilled mortar and
pestle and a phosphate buffer pH 7.5, dried seeds were pulverized.
The supernatant underwent additional salt precipitation before
being cutoff, separated, and utilized to estimate total protein and
antibacterial activity. The sample was stored at -20 in a freezer after
being centrifuged for 15 min at 10,000 rpm. After partial purifica-
tion using the ammonium sulphate precipitation technique, sam-
ples were collected for antimicrobial tests. According to the
findings, germinating seeds of soya, barley, maize, jowar, and
wheat had more antimicrobial peptides that act on gram-positive
and gram-negative bacteria [73].
Sprouting for Isolation of Akhtaruzzaman et al. [74] reported the isolation and characteriza-
Enzymes tion of protease enzyme from leguminous seeds using sprouting/
germination process. According to the mentioned study, legumi-
nous seeds can be a source of proteases for use in industry. Seven
different types of leguminous seeds—soybean, lentil, black gram,
green gram, Bengal gram, groundnut, and pea bean—were used in
the study to identify and characterize the proteases. Temperature
and pH were found to affect protease activity. Maximum specific
activity was seen in the pH profile of proteases between 7.5 and 9.0.
The seeds were cleaned separately and immersed in distilled water
for overnight germination at room temperature. Due to their low
fat content, all seeds were then ground using an electric homoge-
nizer without the use of acetone, with the exception of soybean and
groundnut. To remove the fat, cold acetone was used to homoge-
nize soybean and groundnut. The homogenates were then finely
pulverized and blended for 3 h with chilled 10 mM Tris–HCl buffer
at pH 8.0 containing 2 M NaCl in a pre-chilled mortar. The
extracted mixtures were put through gauge filters, and the filtrates
were centrifuged for 10 minutes at 10,000 rpm below 4 °C. The
estimated extracellular protein content and further purifications
were done using the collected supernatant. For overnight precipi-
tation, the collected supernatants were saturated with 50% solid
ammonium sulphate. After precipitation, they underwent a 30-min
centrifugation at 10,000 rpm at 4 °C. The precipitate that had been
collected was dissolved in 10 nm Tris–HCl buffer (pH 8), dialyzed
against the same buffer, and then centrifuged at 5000 rpm for
356 Gitanjali Sambhajirao Deokar et al.
Sprouting for Isolation of The purpose of this study reported by Sulieman, M.A., 2008, was
Amino Acids to investigate how sprouting affected the cultivars’ chemical, com-
positional, energy, and amino acid contents. Three varieties of
Sudanese lentils—Rubatab, Nadi, and Selaim—were sprouted
over 3 and 6 days. The dried and ground seeds were sprouted. A
determination was made regarding how sprouting altered the prox-
imate makeup and amino acid content. While food energy and
Nitrogen Free Extract (NFE) dropped during sprouting. The
amino acid content of the seeds after sprouting was observed to
change, and it was found that there was a little variance between
cultivars. For the Selaim cultivar, sprouting for 3 days increased the
proportion of all essential amino acids, with the exception of
methionine, and decreasing amino acid content was shown when
the sprouting duration was extended to 6 days, as was the case for
histidine, lysine, and arginine. This outcome was likewise seen for
the Rubatab cultivar, except for methionine and lysine, where the
amount of essential amino acids rose as a result of sprouting. The
essential and non-essential amino acids were enhanced in the Nadi
cultivar after 3 days of sprouting. All cultivars of lentils generally
had low levels of sulphur amino acids like methionine and cystine.
Each cultivar’s bulk was divided into three equal pieces, the first
of which served as a control (unsprouted seeds), the second of
which was given 3 days to sprout, and the third of which was
given 6 days to do so.
The seeds were steeped in distilled water for 2 h at room
temperature prior to sprouting. In sterile petri dishes lined with
damp filter paper, sprouting was done for 3 and 6 days at 4 °C.
Samples were dried at room temperature at the conclusion of each
sprouting phase and crushed to pass through a 0.4 screen for a
future chemical analysis. For further study, the unsprouted seed
control groups were crushed and stored at 4 °C. The amount of
total nitrogen, crude fiber, and ash in a sample of unsprouted and
sprouted seeds were examined. The study found that the proximate
composition and food energy values of lentil underwent a notable
alteration as a result of germination. Before germination, lentil had
a low concentration of amino acids containing sulphur. Essential
and non-essential amino acid levels increased as a result of
germination [75].
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 357
4.2.1 Preliminary Guide There are two types of fermentation, naturally occurring and inocu-
to Fermentation lated, depending on the source of the bacteria used in the process.
Procedures According to the amount of water in the system, fermentation can
also be classified as either solid-state (SSF) or liquid-state fermen-
tation (LSF) [82–84]. Before fermentation, edible seeds frequently
require pretreatment, such as soaking, cracking, grinding, sifting,
and boiling. [84] These processing techniques are frequently put
together in combination. Prior to natural fermentation, seeds can-
not be cooked or autoclaved since doing so will partially or totally
eliminate any bacteria already present on the seeds. The most
frequent bacteria utilized in edible seed fermentation as starter
culture and inoculum are lactic acid bacteria (LAB), including
Lactobacillus (Lb.) acidophilus, Lb. brevis, Lb. bulgaricus, Lb. casei,
Lb. fermentum, Lb. johnsonii, Lb. paracasei, Lb. plantarum,
Lb. reuteri, Lb. rhamnosus, Lb. rossiae, Lb. Streptococcus (Sc.) ther-
mophilus, Bifidobacterium (Bb.) animalis, Bb. infantis, Lactococcus
(Lc.) lactis, and Weissella (W.) paramesenteroides [81–84]. In addi-
tion, Bacillus (B.) subtilis has also been commonly used to ferment
edible seeds [83]. Additionally, cultures of fungi (molds) used for
fermentation are Aspergillus (A.) oryzae [85], A. awamori, A. sojae,
A. niger, Agrocybe (Ac.) cylindracea, Cordyceps (C.) militaris,
Coprinus (Cr.) cinereus, Grifola (G.) frondosa, Ganoderma (Gd.)
austral, Gd. neo-japonicum, etc. Cultures of yeasts, such as Issatch-
enkia (I.) orientalis, Saccharomyces (S.) cerevisiae, and S. boularidii,
etc., have also been employed to ferment edible seeds [81, 86]. The
amount of inoculum in the starter culture is essential for the fer-
mentation process. Inoculation of 1% to 10% (bacteria (mL)/sam-
ple (mL or g)) of the starting culture (108 cfu/mL) has been used
regularly in SSF and LSF of edible seeds, and their products, with
106 to 107 cfu/mL LAB in original samples, have been used for
LAB fermentation. In SSF of edible seeds for B. subtilis and fungal
fermentation, inoculation of 5% (bacteria (mL)/sample (mL)) of
the starting culture (105/g sample) has been employed most fre-
quently [81, 83]. To carry out the fermentation effectively, the
inoculum needs to be optimized. The fermentation efficiency is
influenced by a number of variables, including fermentation tem-
perature, duration, humidity, and other circumstances [81]. Other
factors controlling the fermentation process which are reported to
be optimized are temperature, humidity, stirring/shaking speed,
aerobic or anaerobic conditions, pH, fermentation time, etc. [81].
Living creatures are profoundly impacted by temperature
variations. The sensitivity of enzyme-catalyzed reactions to minute
temperature variations is very high. As a result, the environment
temperature frequently affects the metabolism of poikilotherms
organisms whose internal body temperature is influenced by it
[87]. Every degree of temperature count. Temperature is key to
fermentation success. The optimum temperature range for yeast
fermentation is between 32 °C and 35 °C. Every degree above this
360 Gitanjali Sambhajirao Deokar et al.
4.2.2 Fermentation for Fermentation is the most prevalent postbiotic source in the food
Isolation of Postbiotics industry. The presence of postbiotics can be found naturally in
several milk-based and other products like kefir, kombucha, yogurt,
and pickled vegetables, etc. [91]. Postbiotics are functional bioac-
tive substances that are produced during fermentation in a matrix
and can be used to improve health. Postbiotics can be thought of as
a catch-all name for all synonyms and related terms of various
components of microbial fermentation. As a result, postbiotics
can consist of a wide range of components, such as metabolites,
short-chain fatty acids (SCFAs), microbial cell fractions, functional
proteins, extracellular polysaccharides (EPS), cell lysates, teichoic
acid, muropeptides derived from peptidoglycans, and pili-type
structures, among others. The use of postbiotics may enable active
bacteria to become more potent or transform them into useful
components. In addition, postbiotics get around the technical
problems of colonization effectiveness and maintaining the
microbes in the product at a high dose. As a result, it is easier to
deliver the active substances where they are needed in the gut, the
shelf life is increased, and perhaps packing and transportation are
also made simpler [92]. The structure and operation of the com-
mensal human gut microbiome can be influenced by postbiotics
produced during fermentation. They also aid in inhibiting possible
pathogens while giving the local microbial population the sub-
strates it needs to produce SCFAs. The following are some poten-
tial advantages of fermented foods and beverages: Kefir’s organic
acids, bacteriocins, carbon dioxide, hydrogen peroxide, ethanol,
and diacetyl all have antimicrobial properties. Kombucha’s low
pH and high acetic acid concentration also inhibit the growth of
pathogens. Meanwhile, conjugated linoleic acid in sauerkraut may
have potential health benefits. Similar types of chemicals are pro-
duced during grain fermentation along with proteolytic activity by
lactic acid bacteria, which transforms wheat proteins into bioactive
peptides (postbiotics). Vitamin B12 is produced during the fer-
mentation of soybeans. Fruit fermentation with Lactobacillus plan-
tarum produces phenolic compounds and a number of organic
acids [93].
362 Gitanjali Sambhajirao Deokar et al.
5.1 Experiments with Sprouted flaxseeds were explored for prebiotic and postbiotic prop-
Sprouted Flaxseeds erties: It was an attempt to develop, In- vitro biorelevant media and
(Linum usitatissimum, time simulation probiotic proliferation methodology to determine
in the Family Linaceae) prebiotic potentials of flaxseed powder. The research ultimately
came up with excellent findings for prebiotic and probiotic poten-
tials of flaxseed. Prebiotic potential of flaxseed powder was tested
using Bacillus coagulans SNZ 1969 marketed probiotic wherein it
was found that flaxseeds act as excellent prebiotic supplement for
the growth of probiotics, similarly at the outset it was also observed
that endophytes from the seeds of flaxseeds colonize in the presence
of MRS agar media, provided strict sterile conditions were main-
tained to avoid environment contamination. It was concluded that
fermented flaxseed powder could be effective postbiotic supple-
ment which could be explored further in postbiotic supplement
development [95].
Table 3
Representative examples of seed fermentation for isolation of prebiotics, probiotics, and postbiotics
Sr.
no. Plant seed Bioactive component Function Reference
1. Hemp seeds (Cannabis Prebiotic potential Ability to support [107]
sativa) probiotics growth was
Probiotics used for observed. Increase in the
fermentation are content of some bioactive
(Lactobacillus compounds like presence
fermentum, of different terpenes that
Lb. plantarum, and inhibit the growth of
Bifidobacterium enteropathogens and
bifidum) high levels of short chain
fatty acids like acetate,
propionate and butyrate
produced during
fermentation that
support the growth of
probiotics
2. Artocarpus integer’s seed Prebiotic potential A. integer extract was found [108]
Probiotics used for to support the growth of
fermentation are probiotics such as
Lactobacillus L. acidophilus and
acidophilus DSM L. casei. The results of the
20079, Lactobacillus present study indicated
casei DSM 20011, and that A. integer extract
Escherichia coli DSM was comparable to the
1103 commercial prebiotics
inulin
3. Red and white rice seeds Probiotic: Lactic acid Gut flora heath booster [109]
bacteria (LAB) stimulate cell-mediated
immunity
4. Fermented finger millet Five potential probiotic Potential in terms of health [110]
flour: Three varieties LAB strains (lactic acid benefits
namely Ravi, Raavana, bacteria) were isolated:
and Oshadha R17 (L. plantarum),
RV02 (L. fermentum)
and RV19 (L. lactis sub
species lactis), RV28
(E. faecium), and O24
(P. acidilactici)
5. Fermented beverage using Postbiotics: Decrease in Enhance the bioavailability [111]
red rice (Oryza sativa antinutrient phytic acid, of minerals, digestibility,
var. Indica, Tapol), increase in phosphorous, and sensory properties of
barley (Hordeum vulgare increase in fibers the final products
L.), and buckwheat (prebiotics), etc.
(Fagopyrum
esculentum),
fermentation culture:
Lactic acid bacteria
(continued)
364 Gitanjali Sambhajirao Deokar et al.
Table 3
(continued)
Sr.
no. Plant seed Bioactive component Function Reference
6. Fermented soybean meal Postbiotics: Product reach Acts as probiotic [112, 113]
using bacillus strains in probiotics, digestible supplement as gut flora
(Bacillus subtilis TP6 peptides, polyglutamic booster and help to
strain) acid, short chain fatty improve innate
acids like lactic acid, immunity, protein
non-reducing content is high, and
oligosacchrides like digestion and absorption
Raffinose, Stachyose, rates are also improved by
etc., isoflavones, low-molecularization of
lipopeptides, protein the proteins.
hydrolysates, and Polyglutamic acid helps
enzymes to reduce body fat
5.2.2 Sprouting A total of 250 g of ragi seeds was taken and cleaned to eliminate
Procedure unfamiliar particles from it. The cleaned seeds were then soaked
into adequate measure of water for 8 h at room temperature. After
8 h, the excess of water from seeds was eliminated utilizing filtra-
tions and the seeds were half dried. The seeds were then kept for
germination for around 24 h. The developed seeds were further
kept for drying. The sprouts on the seeds were shed and cleaned
physically. The seeds were then crushed to get the ragi powder,
passed through sieve number #100 to get uniform particle size.
5.2.3 Fermentation Eleusine coracana sprouted seed powder (30 g) obtained as per the
Procedure above-mentioned procedure was taken, and to it was added to 1 g
of Bacillus coagulans SNZ 1969 powder and 1 g of citric acid
powder. Forty milliliters of water was added to the mixture and
the mixture was placed for 24 h at room temperature. After 24 h of
fermentation, wet mass was extruded through the extruder. The
extrudates are shaped into small spherical granules. The wet gran-
ules were allowed to dry. Methodology: Probiotic proliferation study
of sprouted, non-sprouted, and fermented products was performed
as reported in our own research publication [95].
Plant Seeds: A Potential Bioresource for Isolation of Nutraceutical and. . . 365
5.2.4 Research Sprouted ragi seed powder has been proved to have excellent
Highlights prebiotic activity in comparison to non-sprouted powder. Sprouted
and non-sprouted ragi seed powder shows self-probiotic potential.
Sprouted powder support the probiotic spore and culture growth
in the presence of antibiotic as compare to non-sprouted powder.
Similarly, combined run real time simulated biorelevant media
study with and without enzymes and antibiotic (Azithromycin)
also depicted the prominent growth of the probiotic spore pow-
ders. The study concludes that germination of seed increases prebi-
otic and probiotic potential of seed. Overall results indicated that
ragi seed sprouting and fermentation increase the extraction of
prebiotic components and probiotic endophyte activation. Results
helps to conclude that sprouting and fermentation are the natural
in situ green extraction techniques which could be explored well for
health benefits. Table 4 indicates some representative images for
the ragi seed sprouted powder prebiotic as well as probiotic
potentials.
6 Conclusion
Table 4
Prebiotic and probiotic potentials of Ragi seed (Eleusine coracana) sprouted powder
Sr.
no. Observations Images
1. Environmental negative controls: No growth observed in MRS broth
tube as well as MRS agar plate maintained throughout the study, it
indicates maintenance of strict sterile conditions during the
experimentation
3. Positive growth control: Both MRS broth and MRS agar media
support the growth of Bacillus coagulans probiotic spores
considered for studies
Acknowledgments
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Abstract
Essential oils in their unadulterated form, can be primarily classified into two fundamental chemical
constituents, namely: hydrocarbons, oxygenated and terpenoidal bioactive compounds. The biochemical
characteristics of essential oils exhibit significant variations contingent upon the specific extraction methods
employed. While traditional techniques such as cold pressing, hydro-distillation, and maceration have long
been prevalent, they are not without their drawbacks, such as lower yield, the potential for degradation of
thermolabile compounds, and concerns regarding the environmental impact of solvent usage. In the pursuit
of sustainable and effective extraction, modern methodologies have risen to prominence, including
microwave-assisted, supercritical, and ultrasonic extraction techniques. These innovative approaches have
circumvented the inherent limitations of conventional methods, offering novel possibilities for harnessing
the full potential of essential oils. This chapter offers a brief review of both classical and contemporary
extraction techniques, shedding light on their influence over the biochemical properties of essential oils.
Furthermore, it delves into the promising perspectives of utilizing these oils in for nutraceutical applica-
tions, underscoring their potential for enhancing human well-being.
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_15,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
373
374 Olusegun Abayomi Olalere et al.
Fig. 1 Schematic diagram of a typical cold press extraction of citrus peel [26]
plant samples are unsuitable for cold pressing since they cannot
sustain high mechanical pressure [25]. Furthermore, there is fluc-
tuation or inconsistent moisture content in cold pressing, which
might affect the biochemical activities of the essential oil as
reported by Çakaloğlu et al. [25].
Furthermore, the earliest and easiest technique of extracting
essential oils is the hydro-distillation technique, which begins with
the immersion of the plant sample straight into the extracting
solvent (water) within the reactor and then boiling the entire
mixture. This extraction technique is said to be a one-of-a-kind
approach for extracting oil from plant parts such as tough nuts,
wood, seeds, and hard surface powders. It is commonly utilized for
the extraction of oil that contains hydrophobic matter with a high
boiling point. Because the oils are covered in water, this technique
allows essential oils to be extracted at a controlled temperature
without being overheated [27]. The capacity to separate plant
components under 100 °C is the major benefit of this extraction
process [28]. The hydro-distillation set-up consists of a heater
source, a reactor, a condensation chamber that converts vapor
from the reactor into liquid, and a decanter to capture the conden-
sate and separate the water and essential oils mixture (Fig. 2).
Essential Oils: Sustainable Extraction Techniques and Nutraceuticals. . . 377
water clevenger
water
wa
Essential oil
te
r
water
wa
steam containing
te
r
essential oil
Mixture of
sample and water
Heating mantle
Past and recent studies had modified the use of the maceration
method for the recovery of essential oil from plant sources. Notable
among them are Kowalskia and Wawrzykowskib [35] who
employed an ultrasound-assisted maceration technique to extract
essential oil from thyme (Thymus vulgaris L.) dried leaves. Kowalski
et al. [36] reported the use of maceration techniques as a prelimi-
nary extraction process before ultrasonic processing of essential oil
from peppermint leaves, marjoram herb, and chamomile flowers.
Mariane et al. [37] investigated the recovery of olive oil from
Brazilian pink pepper using different stages of the maceration
process. Soares et al. [38] incorporated the ultrasonic and macera-
tion process for the extraction of enhancing flavoring of rosemary
and basil extra virgin olive oil. Unfortunately, the use of maceration
for extraction of essential oil has many limitations which include a
longer duration for extraction which could take days for comple-
tions [39]. Higher solvent consumption and a low degree of other
drawbacks affect the effectiveness of maceration extraction of essen-
tial oil [39].These limitations reduce the quality characteristics and
hence the biochemical activities of their essential oils. Traditional
extraction methods often take a long time, which means that some
of the plant material’s bioactive components will inevitably
degrade. Examples of these conventional approaches are listed in
Table 1.
Table 1
Conventional methods of extracting essential oils from various plant sources
Conventional
Sample Parts of plant extraction methods References
Pequi (Caryocar brasiliense) Fruit Cold pressing [40]
Rice bran Husk Cold pressing [41]
Cannabis sativa L. hemp Leaves Cold pressing [42]
Fennel Leaves Cold pressing [43]
Prunus serotine Seeds Cold pressing [44]
Clove Buds Cold pressing [45]
Hemp Seeds Cold pressing [46]
Rosmarinus officinalis Whole plant Hydrodistillation [47]
and Origanum compactum
Lamiaceae (Mint) Leaves Hydrodistillation [48]
Kumquat Peels Hydrodistillation, ultrasonic, [49]
microwave extraction
Schinus molle Leaves and fruits Hydrodistillation, fractional [27]
hydrodistillation,
and steam distillation
Bitter orange Peel wastes Hydro-distillation [50]
O. basilicum L. Leaves Hydrodistillation [51]
O. vulgare L. subspecies hirtum Aerial parts Hydro-distillation [52]
Litsea cubeba (Lour.) Pers. Fruits Hydro-distillation [53]
Aquilaria malaccensis Leaves Hydro-distillation [29]
Thymus serpyllum L. herb Leaves Maceration [54]
Brazilian pink pepper Fruit Maceration [37]
Rosemary and basil Leaves Maceration [38]
Orange peels Peels Maceration [55]
4 Conclusion
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Chapter 16
Abstract
Phytochemicals extracted from leaves, fruits, roots, and seeds of plants exhibit high nutraceutical, antioxi-
dant, and antimicrobial potential. Such valuable components can be obtained from natural materials via
extraction, an important parameter in analytical chemistry. Since conventional extractions methods pose
severe environmental threats and have a negative impact on energy economy, moving toward green
strategies is important. Green technologies are ecofriendly and give maximum yield, and the product
obtained are pure and less toxic. Ultrasound, microwave, supercritical fluid, subcritical fluid, pressurized
liquid, enzymatic hydrolysis, radio frequency, electroosmotic dewatering, cold plasma treatment, high-
pressure processing, electrotechnology, ionic liquid, accelerated solvent extraction, and hydrotropic extrac-
tion are some of the methods used in clean and green technologies to extract biologically active components
from plants. This chapter also discusses nonthermal extraction technologies . This chapter on clean and
green technologies, processes, and protocols will provide collective and advanced knowledge to research
community in the food and nutraceutical sectors.
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_16,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
391
392 Insha Arshad et al.
and relatively high pressure, and they may diffuse swiftly through
solid materials, resulting in faster extraction rates. The capacity of a
supercritical fluid to modify its density by altering its pressure
and/or temperature is one of its most crucial characteristics.
Changing the extraction pressure might alter the solvent strength
of the fluid, given that density and solubility are related [7]. This
technology’s expanding industrial utilization is primarily attribut-
able to its selectivity, facility, and separation capacity. According to
Ahmad, Masoodi, Rather, Wani, and Gull (2019), the SFE enables
the extraction of a large number of nutraceutical compounds, many
of which are impossible or impractical to extract using conventional
methods or whose purification requires high resolution columns,
which are not always available on the national market, thereby
making their use very expensive [8]. Supercritical extraction is
often used to separate nonpolar bioactive components (carotenoids
and lipids) since the solvents used in this technique are nonpolar.
One alternative is the extraction of polar compounds like flavonoids
using modifiers like ethanol, methanol, water, and acetone
[9, 10]. Less viscosity and a shorter extraction time lead to an
improvement in the diffusion and mass transfer of the crucial fluid
[1, 11]. Table 1 shows the extraction of various bioactive com-
pounds by supercritical extraction. Factors such as temperature,
pressure, and other inherently changeable features, as well as
some extrinsic factors like the properties of the supercritical fluid,
all affect SFE: interactions with specific analyzers, the sample
matrix, and various environmental factors [6].
Table 1
Extraction of phytocompounds via supercritical fluid extraction methods
2.2 Subcritical Fluid Subcritical fluid extraction is an ecologically friendly and perfect
Extraction method that is used in selective extraction operations, in the treat-
ment of agro-food waste, and in industries to manufacture safe and
high-quality products [19]. According to Cravotto et al. (2022)
subcritical, near-critical, or pressurized hot water are all terms used
to describe this technique, in which water is subjected to adequate
pressures (generally 10 to 100 bar) between 100 °C and a critical
temperature of 374 °C (often between 100 and 250 °C)
[20]. Researchers have documented the utilization of supercritical
fluid and their liquid counterparts as appropriate solvents. This
approch not only yields the highest amount of value added nutra-
ceuticals but also represent a sustainable and environmentally
friendly processing method. It serves as a substitution for hazard-
ous organic solvents with more ecologically sound alterna-
tive [21]. In contrast to “supercritical” fluids, “subcritical” fluids,
also known as pressurized liquids like water and ethanol above their
boiling points but below critical temperatures, show good solvency
properties for the extraction of a variety of biological moieties
present in matrices made from agricultural sources. Some of the
drawbacks of supercritical fluids, such as poor affinity of carbon
dioxide for polar solutes and high capitalization costs of the pro-
cess, are alleviated by the use of subcritical fluids. Subcritical water
has been used to extract essential oils with effectiveness [22]. The
use of water being ecologically friendly, the ability of extracting
more rapidly with less amount of solvents, and the ability to pro-
duce higher yields make subcritical water superior to standard
organic solvents (Fig. 2) [19]. Solubility and mass transfer are the
two most important variables in subcritical solvent extraction [23].
High Selectivity
Advantages of
Low viscosity Subcritical fluid High Diffusivity
With values that fall between methanol and ethanol, the dielec-
tric constant of water decreases from 80 to about 30 due to the
weakening of hydrogen bonds, which makes the efficient extraction
of moderately polar and nonpolar target compounds possible.
Some advantages of subcritical fluids are summarized in Fig. 2 [20].
2.4 Modes of This extraction method has two primary modes: static extraction
Extraction and dynamic extraction. In static extraction, to retain water in a
liquid form, subcritical water is combined with the sample to be
extracted in an extraction vessel and heated to an appropriate
temperature under light pressure. Once extraction is completed,
the extractant is collected for chromatographic examination. This
extraction method is comparable to rapid solvent extraction and its
efficiency typically falls short of dynamic extraction’s efficiency.
Green and Clean Extraction Technologies for Novel Nutraceuticals 397
Table 2
Extraction of different compounds by using subcritical fluid extraction technique
3.1 Working Handling liquid sample requires their conversion into the solid due
Principle to the absence of commercial kits, achieved by adding adsorbent or
adsorbents. The efficiency of the system is influenced by thermody-
namic and kinetic parameters, with three interconnected processes
playing a crucial role: mass transfer, matrix effect and
solubility [35].
Table 3
Extraction of different compounds via pressurized fluid extraction
4 Ultrasound-Assisted Extraction
Table 4
Extraction of different compounds via ultrasound-assisted extraction
4.2 Factors Affecting Factors that impact extraction efficiency alone or in combination
the Extraction were investigated. They are as follows:
I. The type of tissue being removed and where in respect to
tissue structures the components are to be removed.
II. The tissue is prepped before being extracted.
III. The characteristics of the components being extracted.
IV. Ultrasonic impacts, which primarily cause superficial tissue
disruption increasing surface mass transfer, enhancing intra-
particle diffusion, loading substrate into the extraction
chamber; improved extractable component yield.
V. Higher extraction rates, particularly early in the extraction
cycle, result in considerable time savings and higher proces-
sing throughput [4].
5.1 Types of MAE MAE vessels are classified into two types, closed and open. Both
systems have four common components, which are listed below: a
microwave generator that works by using magnetron to generate
microwave radiation; a waveguide through which microwave
spreads to microwave cavity; a circulator that allows the microwave
to change ahead; and an applicator to perform the test [62].
5.2 Instrumentation Mono- or multimode microwave oven cavities are created. The
and Mechanism of monomode cavity, which stimulates just one mode of resonance,
Microwave Extraction can produce a frequency. The sample may be positioned at the
electrical field’s maximum since it is known how the field is
distributed. The size of the multimode cavity raises the possibility
that the incident wave will affect several modes of resonance. The
field can be homogenized by the superimposition of modes. Sys-
tems such as rotating plates are utilized for homogenization
[63]. Modern techniques like MAE warm the solvent with micro-
wave energy and release the plant extractable compositions into an
aqueous phase. Although mass transfer for convention and MAE
takes place in the same direction, they are different because energy
is lost volumetrically during the MAE process inside the illumina-
tion medium. The power of the microwave and the material’s
dielectric loss factor both affect how quickly temperature rises
during microwave heating. Veggi et al. (2013) state that numerous
interactions must occur during the solid-solvent extraction phase of
the MAE process [64]:
• The solid matrix’s contact with the solvent
• Component breakdown or solubilization
• Moving the solute away from the solid matrix
• The solute’s transition from the solid’s surface to the bulk
solution after being extracted
• The extract’s motion in relation to the solid
• Disposal of the extract and solids after separation
As a result, the solvent effectively diffuses into the solid matrix
and the solute disintegrates up until it reaches a concentration that
is constrained by the solid’s physical features [65]. Stability, trans-
formation, and dissemination are the three steps that help compen-
sate the extraction process. Solubilization and partition control the
way the substrate is taken from the outer surface of the subatomic
particle during the equilibrium phase. There are transitional stages
before dissemination. At the solid-liquid interface, mass transfer
encounters resistance; at this point, convection and diffusion are
the dominant modes of mass transfer. The solute must get past the
interactions holding it to the matrix in the final stage in order to
enter the extraction solvent [64, 66]. The closed MAE system is
widely employed for extraction under harsh conditions, such as
Green and Clean Extraction Technologies for Novel Nutraceuticals 405
5.2.1 Focused A Soxhlet apparatus with variable heating power was used to per-
Microwave-Assisted form FMAE at 2450 MHz and atmospheric pressure. A quartz
Extraction System (FMAE) extraction tank containing solvent is filled with powdered and
air-dried sample matrix. Once the container had reached room
temperature, the extracts were centrifuged, and the supernatant is
collected and dried by vacuum evaporation. This can manage a
large amount of sample material and an additional reagent may be
added at any time during the process of extraction [67, 68]. Table 5
shows the extraction of various nutraceuticals by MAE at different
conditions. Figure 6 shows the microwave-assisted extraction’s
instruments; the power control system and frequency control sys-
tem adjust the intensity of microwave energy applied to the sample.
The sample holder material should be transparent and distant to
thermal and chemical degradation and should be transparent [67].
5.2.2 Dynamic MAE A dynamic MAE system developed by Ericsson and Colmsjo in
2000 generated extract with yields comparable to those of Soxhlet
extraction but in a lot less time. The dynamic microwave extractor
comprises the solvent supply system, microwave oven, extraction
cell, temperature set point controller with type K thermocouple,
fluorescence detector, and fused-silica restrictor [67].
6 Hydrotropic Extraction
Table 5
Extraction of different compounds via microwave-assisted extraction
Fig. 6 Flow designs of focused (a) and dynamic (b) microwave-assisted extraction
6.1 Hydrotropic The term “hydrotropy” was first utilized by Carl A. Neuberg in
Agents 1916 [79]. He used the term “hydrotropic agents” for anionic
organic salts, which increase the miscibility of less-soluble solutes
in aqueous solutions at high concentrations. These compounds are
amphiphilic molecules with a short or branched alkyl chains
attached to ionic or polar groups for hydrophilicity while sulfate,
sulfonate and carbonate group confer hydrophobic characteristics
[78]. Most commonly used hydrophytes are xylene, polyhydroxy
benzene, toluene sodium salts of lower alkanols, aromatic acid
derivatives, sodium alkyl benzene sulfonates, etc. Some neutral or
cationic aromatic derivatives are also used as hydrotropic agents,
but these are rarely available [80]. As hydrophytes have both
hydrophobic and hydrophilic moieties, they are compared to sur-
factants, but the presence of short chain hydrophobic moiety dis-
tinguishes them from surfactants. Therefore, they are sometimes
called short chain surfactants or salting agents. Some hydrotropic
agents are used for selective extraction of nonpolar phytofragments,
which are water insoluble by cell permeabilization [81]. The struc-
tures of some hydrotropes like sodium toluene sulfonate, sodium
xylene sulfonate (SXS), sodium benzene sulfonate, sodium cymene
sulfonate, and sodium cumene sulfonate are shown in Fig. 7.
6.2 General Many theories have been proposed for describing the mechanism of
Mechanism of Action action of hydrotropic agents. The extensive study led to various
perspectives, and their finding were summarized in three
approaches regarding the mechanism.
1. In the first approach, hydrophyte and solutes forcefully interact
to form hydrophyte-solute complexes [80]. The phospholipid
bilayer of plant cell wall is destructed by hydrophytes, after
which the hydrophytes penetrate the inner structure of the
plant cell. When immersed in aqueous medium, the effect of
hydrophytes on cork cells is very minimal. The cork cell wall
contains cellulose and suberine lamellas. Suberine lamellas
make cork cells impermeable to water. Hydrotropic solution
opens these water-impermeable suberine lamellae and then
breaks down the mature cork cells. The cork cell layer is dis-
turbed by hydrotropy, and the aqueous solution penetrates the
408 Insha Arshad et al.
cell wall. When the hydrotropes solution enters the cell cyto-
plasm, the cells swell, releasing them from closely coupled
structures and hydrotropic solution cause precipitation of sol-
ute.. Therefore, the instantaneous recovery of dissolved solutes
from solutions diluted with aqueous solution is viable [82].
2. In the second mode of action, hydrophytes are considered as
“structure breakers and structure makers” as they alter the
solute structure by inserting themselves into water
structure [83].
3. The most widely accepted mechanism for hydrotropic extrac-
tions is the ability of hydrophytes to act as micelle structures at
a particular concentration. When diluted with distilled water,
the hydrotropic solutions cause the bioactive chemicals to pre-
cipitate out of the solution, making it possible to obtain the
extracted solute with ease [84].
6.3 Advantage and Advantages of hydrotropic extraction are its nontoxicity and easy
Disadvantages accessibility. Hydrotropic solvents have some characteristics that
would appeal to modern researchers’ tastes. Hydrotropic solvents
have made a noteworthy mark as a smart choice for phytochemical
extraction, thanks to their toxic-free, chemically inert, affordable,
accessible, temperature- and pH-independent, and high selectivity
properties. In addition to having a high extraction efficiency, pure-
ness, and quality of the crystalline product, this environmentally
friendly solvent can be recycled numerous times with a comparable
extraction efficiency [78]. Some disadvantages regarding this
Green and Clean Extraction Technologies for Novel Nutraceuticals 409
technique are its poor recycling ability. Water dilution during recov-
ery and reuse creates a large amount of aqueous hydrotropic solu-
tion that needs to be reconcentrated for recycling
[85]. Additionally, the majority of the investigations concluded
that high hydrotropes concentrations are necessary to accomplish
high phytochemical solubilization, which necessitates the con-
sumption of a sizable quantity of hydrotropes salts in order to
create highly concentrated hydrotropic solvents. Most importantly,
there is uncertainty over how efficiently a hydrotropic agent will
interact with the intended solute.
6. Electro-osmotic Dewatering
In recent era, there is a great interest in electro-regulated food-
processing techniques and their use in the extraction of nutraceu-
ticals. In electro-osmotic dewatering, the moisture of food is
removed at low electrical field and is controlled by the electrical
resistance present in the system to maintain specific conditions.
Electro-osmotic dewatering is basically a drying method and has
recently become quite popular in the nutraceutical business. To
extract moisture from plant materials and food, electro-osmotic
technique employs an electric field of approximately 5–30 volts.
This process is better than the traditional heat drying methods since
it can reduce carbon emissions by about 80%. Furthermore, energy
consumption is reduced up to two-thirds in this technique as
compared to traditional thermal processes. The basic principle
followed by this technique is osmotic dehydration, as it is a drying
process, and enhanced mass transfer. An electrochemical double
layer is formed on the interface of aqueous suspension due to the
applied mechanical pressure. This mechanical dewatering leads to
the drying of substrate [93]. Since electro-osmotic dehydration is
frequently used to concentrate fruit fragments and achieve
improved jam properties on difficult-to-dewater substrates, it
would be excellent to employ it to treat high-sugar fruits and
vegetable by-products that contain labile antioxidant and surface
colorants. Additionally, if the substance is elastic and well grained, it
is too delicate to treat and too viscous to pump, making water
removal more difficult. Prior to industrial deployment, this issue
of electro-osmotic dewatering should be overcome [94].
6.5 Design and Direct current (DC) is used to impart an external electrical field to a
Working Principle semisolid material sandwiched between two electrodes, resulting in
electrical dehydration (ED). When dewatering proceeds downhill
in a bed of semisolid material where the initial water content is
uniform across the bed, the water content in a section of the
material close to the top electrode opposing the drainage surface
decreases regionally. The higher electrode and the dewatered mate-
rial now have a greater electrical contact resistance. To effectively
apply electro-osmotic dewatering to various types of materials, it is
essential to increase the dewatering rate, decrease the final water
content, and utilize the least amount of energy feasible to remove
the water. Electrical dehydration (ED) differs from mechanical
dewatering in that it does not employ fluid pressure, compressive
forces, or centrifugal forces. The process of electro-osmotic dewa-
tering is elaborated in Fig. 8. It offers several advantages over
mechanical procedures, particularly in effectively dewatering colloi-
dal particles, gelatinous substances and solid-liquid mixture based
on biological components, which mechanical techniques may
struggle to adequately adress.
412 Insha Arshad et al.
Solvent
Composition
Extraction
Solvent to
time and
Feed Ratio
Cycle
Factors
Effecting
Microwave
Temperature
Power
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Chapter 17
Abstract
Optimization is the selection of the most efficient system that can resolve and help in attaining the objective
functions by designing or operating various optimized procedures. In this chapter, optimized extraction of
nutraceuticals is discussed. With an increasing demand for nutraceuticals, there is now greater focus on
nutrapharmaceutical industry that produces safer natural products/extracts in a sustainable manner by cost-
effective and eco-friendly green extraction routes. So the strategies that need to be devised for this purpose
include the evaluation and optimization of various extraction variables (particle size, material/solvent ratio,
extraction time and cycle, type of extraction technique, extraction conditions like temperature, agitation
rate, etc.) that aim to control the stability of the bioactives and achieve the sustainable quality of the end-use
nutraceutical products. In this chapter, we have focused on the optimized extraction of nutraceuticals along
with the recent technological trends that are applicable toward the recovering of best possible levels of such
high-value components.
Key words Optimized extraction, High-value components, Bioactives stability, Green extraction,
Sustainable quality, Healthy products, Nutrapharmaceuticals
1 Introduction
Plants have always served human beings as a source of food and folk
medicine, as well as they offer a platform for isolation of lead
molecules for development of modern drugs. However, in consis-
tent with the notion “let your food be your medicine,” currently
there is a renewed interest on the use of plants as a source of food
and medicine. In line with the concept of optimal nutrition, cur-
rently, the science of functional food and nutraceuticals is an
emerging area in food science [1–3]. In fact, a huge number and
kind of plants, especially herbs, spices, food crops, and medicinal
species have been explored for isolation of a broad range of bioac-
tives and high-value phytochemicals with biological and nutraceu-
tical potential [2–5].
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_17,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
419
420 Shanza Malik et al.
Dietary
supplements
(co-enzyme Q ,
Carnitine)
Terpenoids
Functional
(carotenoids,
foods
modo-terpenes,
(probiotics,
Phyto-steroids)
pre-biotics) Nutraceuticals
(nutrition &
pharmaceuticals)
Polyphenols
(anthocyanins, Micronutrients
flavones, (gallic acid)
stilbenes,
isoflavones)
Micronutrients
(vitamins,
minerals)
2.1 Selection of Choosing the source material for nutraceutical extraction is quite
Source Material challenging and critical. The yield and makeup of bioactive chemi-
cals can be influenced by elements like plant species, the portion of
the plant that is used (leaves, roots, seeds, etc.), and the maturity
stage. The main source materials used for nutraceutical extraction
are shown in Fig. 2.
Additionally, the geographical origin of the starting material
and the variation in chemical structure within the identical species
can have an impact on the success of the extraction. Numerous
aspects, including the presence of bioactive chemicals, accessibility,
sustainability, safety, and legal and regulatory considerations,
should be taken into account when choosing the material sources
for extracting nutraceuticals [10].
Here are some typical sources that are frequently utilized to
extract nutraceuticals:
(a) Plants: Numerous dietary supplements, such as vegetables,
fruits, herbal remedies, and medicinal plants, are obtained
from plants. Examples include Ginkgo biloba extract, curcumin
from turmeric, resveratrol from grapes, and the caffeine in
green tea extracts derived from Camellia sinensis.
(b) Marine sources: Marine life like algae, seaweed, and some fish
can be great sources of dietary supplements. Fish oil–derived
fatty acids known as omega-3 (eicosapentaenoic acid/EPA
and docosahexaenoic acid/DHA) are frequently used as
nutraceutical supplements.
424 Shanza Malik et al.
Table 1
Different types of nutraceuticals and their sources [29]
Nutraceutical
compounds Chemical structure Sources
Lycopene Plant sources,
tomato
Vitamin D3 Marine
organism,
fishes
Curcumin Turmeric
Procedure
The general steps involved in this procedure are briefly described
below and shown in Fig. 5 [40]:
I. Preparation of sample: The first step is the preparation of
the sample material. It involves cleaning and drying the raw
material to remove impurities and moisture. The sample
may also need to be ground or chopped into smaller pieces
to increase the surface area for better extraction.
II. Solvent selection: Next, an appropriate solvent is selected
based on the target compounds to be extracted. The solvent
should have good solubility for the bioactive components
and be safe for human consumption. Common solvents
used in UAE include water, ethanol, methanol, and their
mixtures.
III. Sample-solvent mixing: The prepared sample material is
then mixed with the selected solvent to create a homoge-
nous mixture. The ratio of sample to solvent can vary
Optimization of Nutraceuticals Extraction 435
Usually, the heating process lasts below 2 min. After receiving more
radiation, the sample is removed for a certain period of time, often
between 10 and 30 min. The samples are given time to cool back to
a temperature that is safe to handle while the extraction is finished
[42, 43].
6.3 Optimization of Enzyme-assisted extractions are known for their optimized results
EAE and conditions. Several studies have shown recently that EAE
provides optimal yield when used with response surface methodol-
ogy with different experimental designs [26, 33, 34]. For instance,
by using EAE with response surface methodology and by optimiz-
ing variables such as temperature, pH, and solvents, a maximum of
proteins was extracted from sugar beets as enzymes are very specific
in nature [50].
440 Shanza Malik et al.
7 Case Studies
7.1 Extraction of The red stigmas of Crocus sativus L. are used to make saffron, the
Saffron most expensive spice in the entire world. Saffron contains roughly
10% moisture, 12% protein, 5% fat, 5% minerals, 5% crude fiber, and
63% carbohydrates, containing starch, reducing sugars, gum, pec-
tin, pentosans, and dextrin (w/w%). Saffron has also been shown to
contain traces of thiamin, riboflavin, and fatty acids such as palmitic,
linoleic, stearic, oleic, and linolenic acids [54].
The three main bioactives of saffron—crocin, picrocrocin, and
safranal—are extracted in an optimized way by using response
surface process. The extraction process variables include the tem-
perature (5–85 °C), extraction time (2–7 h), and ethanol concen-
tration (0–100%). The three bioactives (picrocrocin, safranal, and
crocin) were detected spectrophotometrically with highest absor-
bance values at 257, 330, and 440 nm, respectively. The final data
were fitted using four models: linear, linear squares, linear interac-
tions, and full quadratic. As anticipated, the whole quadratic model
had the highest R2 values for the picrocrocin, safranal, and crocin
concentrations, respectively, at 83.91%, 86.60%, and 92.42%. Our
findings showed that short durations, high temperatures, and mod-
erate ethanol concentrations had the greatest influence on the
chemical extraction efficiency. An ethanol content of 33.33%,
extraction period of 2 h, and extraction temperature of 85.0 °C,
respectively, were observed. Under these conditions, the observed
empirical values E1 for picrocrocin, safranal, and crocin were
1190.47, 474.02, and 2311.68 , whereas the theoretical values
were 1237.27, 652.08, and 2821.23 [55].
Table 2
Comparison of different extraction processes [53]
Solvent
Extraction Sample vol.
Techniques Description time (min) size (g) (mL) Cost Advantages Disadvantages
Shanza Malik et al.
Solvent Solvent is heated in conventional oven 6–8 1–20 10–100 Moderate Rapid and easy handling High solvent consumption,
extraction and passed by sample thermal degradation,
long treatment time
Microwave- Immersion of the sample in solvent and 3–30 1–10 10–40 Moderate Rapid, easy to handle moderate solvent Extraction solvent must
assisted microwave energy is submitted consumption absorb microwave energy
extraction Filtration step required
Supercritical A high-pressure vessel is filled with 10–60 1–5 30–60 High Rapid, low solvent consumption, Many parameters to
fluid sample and crossed continuously by concentration of extracts, no filtration optimize
extraction the supercritical fluid necessary, possible high selectivity
Ultrasound- Immersion of the sample in solvent and 10–60 1–30 50–200 Low Easy to use Large amount of solvent
assisted submission to ultrasound using a US consumption, filtration
extraction probe or US bath step required
Pulsed electric Pulses of high electric voltages are 5–10 10–50 10–100 High Rapid and non-thermal process Mechanism not well known
field applied to the sample placed in and process
extraction between two electrodes intensification is difficult
Pressurized Heat of the sample by a conventional 10–20 1–30 15–60 High Rapid, no filtration necessary, low solvent Possible degradation of
solvent oven and crossed by the extraction consumption thermolabile analytes
extraction solvent under pressure
High Sample is pressurized (100–1000 MPa) 1–30 10–20 10–50 High Rapid, green technology, high selectivity, High cost equipment
hydrostatic through a pressure transmitter liquid high extraction yield, no degradation of
pressure target molecules
extraction
Optimization of Nutraceuticals Extraction 443
7.1.2 Extraction Due to their many benefits, green extraction techniques and sol-
Parameters vents have recently attracted growing interest. This study looked at
how different bioactive compounds may be extracted from bee
pollen by using ultrasonic methodology and polar aprotic solvents
(DESs). In this regard, response surface methodology was used to
examine the overall effects of process variables on individual amino
acids, organic acids, and phenolic compounds. These variables
include molar ratio of the DES (1, 1.5, and 2), sonication duration
(15, 30, and 45 min), and ultrasonic power (90, 135, and 180 W)
(RSM). A molar ratio of 2, a sonication duration of 45 minutes, and
an ultrasonic power of 180 were discovered to be the ideal para-
meters. The control group was composed of extracts produced by
the maceration process using ethanol as a solvent. The total indi-
vidual amino acid and total individual organic acid levels utilizing
DESs were greater than those in the control group. Additionally,
when utilizing DESs as opposed to controls, substances like myr-
icetin, kaempferol, and quercetin were extracted at higher amounts.
Antimicrobial activity testing revealed that the DES groups had a
wide range of antibacterial activities against each and every one of
the bacterial species tested. However, this inhibitory effect was
incredibly weak in yeast-like fungi samples. The study for the
extraction of saffron is the first to assess how DESs affect bee
pollen’s ability to extract beneficial compounds. The outcomes
demonstrate the applicability of this novel and environmentally
friendly extraction method and solvent (ultrasonic extraction/
DES) [58].
444 Shanza Malik et al.
7.2 Extraction from Ziziphus lotus are pulpy fruits that are valued for their particular
Fruit of Ziziphus lotus flavor, nutritional value, and therapeutic uses and are consumed as
food all over the world. The abundance of bioactive chemicals in
this fruit is thought to be responsible for its useful characteristics.
Unfortunately, despite ideal extraction conditions, the extraction of
these chemicals and their underlying phytochemical characteriza-
tion has been rarely studied. In this study, Z. lotus fruit pulp extracts
were obtained employing heat-assisted extraction method and
response methodology. These extracts obtained were rich in bene-
ficial biocompounds in terms of their compositional and nutraceu-
tical potential [59].
7.2.1 Extraction The optimal conditions were noted to be as follows: time, 71 min;
Parameters temperature, about 50 °C; solid to solvent ratio, 1:60 (g/mL); and
ethanol concentration, 50%. This gave 48.62% output, includ-
ing 106.64 milligrams of Gallic acid equiv [31]/gram dry matter
of reducing ability with the Folin-Ciocalteu (FCR) reagent, and
49.65 mg of quercetin equiv (QE)/g DM of total flavonoid (TAA).
A total of 38 substances were discovered utilizing LC-ESI-MS/MS
analysis using these parameters. Results also revealed that the opti-
mized pulp extracts from Z. lotus fruit exhibited good antibacterial
activity. The pulp can be utilized to extract bioactive chemicals that
can be employed as ingredients in functional foods and nutraceu-
ticals, and this study offers crucial information on their potential
application [60].
7.3 Extraction from The Rubus genus has an extensive record of medicinal use with
Rubus ellipticus notable therapeutic effects in treating the liver and kidney meri-
dians. In China, its roots and bark are used to relieve lower back
pain, enhance vision, and prevent uterine, cervical, and colon can-
cer. The genus has a number of species that are employed as anti-
microbials, anticonvulsants, muscle relaxants, radical scavengers
and used in the treatments of ulcers, gastrointestinal issues, diabe-
tes, and inflammation. Although the potential of nutraceutical and
functional food derived from Rubus ellipticus fruit is well estab-
lished, there are no comprehensive research works on the optimi-
zation of extraction procedures for increasing yield. Plackett-
Burman (PBD) and Central Composite Design were used in the
current work to extract bioactive chemicals (CCD).
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Optimization of Nutraceuticals Extraction 447
Abstract
In recent years, application of the computational approach, a predictive tool, in food and nutritional
sciences has outweighed classical analytical methods. The sophisticated informatics approaches such as
chemo-informatics and bioinformatics methods are integrated with the food industry for the extraction and
identification of bioactive compounds. Model simulation of the molecule and the assessment of the
dynamics are frequently used to study the structure and function of food carbohydrates, lipids, and other
small molecules. Beyond the simulation, current advancement in algorithms has solidified machine learn-
ing’s ability to predict the availability of the functional component and its biomolecular activity. The chapter
summarizes the joint applications of bioinformatics and simulation methods in the extraction and discovery
of bioactive and nutraceutical components, in particular, the selection of analytical procedure, activity
prediction, docking, and physicochemical properties.
1 Introduction
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science, https://doi.org/10.1007/978-1-0716-3601-5_18,
© The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer Nature 2024
449
450 Prabina Bhattarai et al.
Table 1
Database for chemicals
No. of
Database Availability compound Link Reference
Generated databases- Free 166.4 billion https://gdb.unibe.ch/downloads/ [13]
17
Zinc 20 Free 1.4 billion https://zinc20.docking.org/ [14]
PubChem Free 112 million https://pubchem.ncbi.nlm.nih.gov/ [15]
ChemIDplus Free 4,00,000 https://chem.nlm.nih.gov/ [16]
chemidplus/
Table 2
Database for bioactive compound
No. of
Database Specification molecules Link Reference
Carotenoids Carotenoid structure, structural isomers 1204 http://carotenoiddb. [20]
database and stereoisomers, chemical jp/
fingerprint
ChEMBL Bioactive compounds with drug-like 2.3 https://www.ebi.ac. [21]
properties million uk/chembl/
PADFrag Biological-functional molecular 5919 http://chemyang. [22]
fragments ccnu.edu.cn/ccb/
database/
PADFrag/
FooDB Physicochemical data, sensory 28,000 https://foodb.ca/ [23]
information (color, flavor, aroma), its
concentration effects on other
attributes of food, physiological
effect, and impacts on human health
Ambinter Structure, biological target 38 million https://www. [24]
ambinter.com/
BIOFAC Compounds from the plants, fungi, and 400 https://biofacquim. [25]
QUIM propolis of Mexican origin herokuapp.com/
NPASS Connects natural products with the 35,032 https://bidd.group/ [5]
biological targets NPASS/
BioPhytMol Anti-mycobacterial phytochemical 2582 https://ab-openlab. [26]
information csir.res.in/
biophytmol/
BIOPEP- Bioactive peptides, quantitative 4540 https://biochemia. [27]
UWM parameters of bioactive fragments, uwm.edu.pl/
SMILES code biopep-uwm/
AHTPDB Antihypertensive peptides 6000 https://webs.iiitd.edu. [28]
in/raghava/
ahtpdb/
Computational Approach and Its Application in the Nutraceutical Industry 453
deep into the first principle of organic chemistry. GDB has subsets
and focuses on the specific spectrum of the compound, such as
FDB17b on the fragment, GDBMedChem on medicinal chemistry
[17], GDBChEMBL on ChEMBL-like molecule [18], and GDB4c
on novel 3D-shaped molecules with quaternary centers [13].
ZINC 20 is a free database hosted by Irwin and Shoichet
laboratories of the University of California, which harbors informa-
tion (docking, 2D, and 3D models) of more than 509 million
purchasable compounds and analogs of over 750 million com-
pounds with a constant update of billions of new molecules [14].
PubChem is the largest chemical database comprising informa-
tion such as 3D structures, biological assay descriptions, and results
of more than 112 million compounds, 298 million substances, and
301 million bioactivities. Compared to other databases, it is more
user-friendly due to its simple and alternative views via dedicated
web pages and presents data related to genes and diseases associated
with the pathway, biological activity, protein, and patent [15].
ChemIDplus is a free web-based search system with more than
4,00,000 chemical records containing over 3,00,000 chemical
structures. This chemical record aids in the identification of the
compounds by providing structure and nomenclature authority
files from the National Library of Medicine (NLM), US states,
and its federal agencies, along with other scientific sites. ChemID-
plus have two versions, ChemIDplus Lite and ChemIDplus
Advanced, on which the latter has additional information regarding
molecular formula, classification code, chemical structure, physical
property, toxicity, and locator code searching [16]. It has been
scheduled to move to PubChem in December 2022 [19].
Carotenoids Database is a repository for 1204 natural carote-
noids from 722 sources of organisms. It contains data regarding the
classification of carotenoid structure, structural isomers, and
stereoisomers, chemical fingerprint which describes the carote-
noids’ chemical substructure, and the details regarding modifica-
tion and eases prediction of the biological function of provitamin A,
membrane stabilizers, allelochemicals, odorous substances, anti-
proliferative activity against the cancerous cell, and reverses multi-
drug resistance (MDR) activity against cancer cell [20].
ChEMBL is a database that harbors information curated from
the primary medicinal chemistry research literature and multiple
other sources. In addition, it contains information regarding the
compound’s bioactivity, molecules, target, and other drug data. Its
web services are built on a RESTful architecture which allows users
to access data programmatically and is also available via other
sources, such as PubChem BioAssay and BindingDB [21].
PADFrag database, which is for a bioactive molecular frag-
ment, holds 1652 FDA-approved drugs, 1259 agricultural chemi-
cals, and 5919 molecules generated from the mentioned drugs and
chemicals. This database consists of physicochemical properties, 3D
454 Prabina Bhattarai et al.
(pork, fish, chicken, milk, egg, etc). Besides these, the database
withholds information regarding structure (tertiary and second-
ary), inhibitory concentration (IC50), toxicity, bitterness value,
source, purification method, and log value of inhibitory concentra-
tion (pIC50) information [28].
A number of deserted databases are not maintained anymore or
might be maintained poorly. In some cases, the wrong interpreta-
tion might occur due to the lack of a definite standard for stereo-
chemistry and aromaticity, leading to new versions of the same
molecules. The current misrepresentation of “Publish or perish”
has adversely flourished among researchers, guild-leading to the
spawn of databases that have a dire chance of getting maintained
after a certain time of publication.
3 Biomedical Informatics
3.1.2 Application The application of the QSAR technique involves the development
of QSAR of a QSAR model, where a set of numerical descriptors related to
the structure of interest serves as independent variables, while the
targeted biological activities are the dependent variables. Then, the
relationship between the dependent and independent variable is
built using multiple linear regression (MLR), partial least square
(PLS) regression, support vector machine (SVC), artificial neural
network (ANN), etc. [31, 32]. For instance, there are many amino
acid descriptors, such as hydrophobicity, bulkiness/molecular size
and electronic property of amino acids, isotropic surface area, and
electronic charge index [32, 33]. However, the properties of amino
acids described by a single parameter are more complicated as they
have less explanatory power and neglect the relationship between
456 Prabina Bhattarai et al.
3.1.3 Antioxidants Antioxidant peptides play a significant role in preventing and treat-
ing various diseases due to their capacity to scavenge free radicals
and prevent oxidative stress [37]. It is essential to determine the
dynamics between human physiology and bioactivity of antioxi-
dants. QSAR has the potential to explore the dynamics and forecast
the interaction between food-derived antioxidant and physiology.
Specifically, QSAR study is focused on dipeptides and tripeptides as
they are absorbed intact from the intestinal lumen to produce
biological effects at the tissue level [38]. Dent et al. 2019 con-
ducted a QSAR study on two datasets of antioxidant tripeptides
where the first dataset contained 214 artificially designed tripep-
tides, and the second dataset contained 72 Beta-lactoglobulin tri-
peptides. The study used 16 amino acid descriptors to conduct
model population analysis (MPA), which improves prediction abil-
ity and interpretability by forming multi-model clusters [39] with
higher cross validated coefficient of determination.
3.1.4 ACE-Inhibitory Several studies have been conducted on identifying and isolating
Peptides several ACE-inhibitory peptides derived from food. Application of
QSAR modeling has identified the novel ACE inhibitory peptides
derived from Qula casein hydrolysates using a two-enzyme combi-
nation. The QSAR model involved amino acid descriptors as pre-
dictors and log transformed IC50 values as the dependent variable.
Amino acid descriptors include five z-scale descriptors where z1
represented lipophilic properties, z2 represented steric properties,
z3 represents electronic properties, and z4 and z5 were related to
other properties like electronegativity, the heat of formation, and
electrophilicity. Finally, the QSAR model was analyzed by SIMCA-
P software (Umetrics, Umeå, Sweden) using partial least squares
regression (PLS). The study also concluded that the peptides pro-
duced by utilizing thermolysin + alcalase exhibited stronger ACE
inhibitory function [40].
3.1.6 Molecular Docking The molecular docking process includes predicting the molecular
orientation of a ligand within a receptor and calculating their
complementarity interaction (binding affinity) using a scoring func-
tion. Molecular docking allows for studying the behavior of pep-
tides in the binding site of target proteins. It is also called a
structure-based method that allows it to determine the structure-
activity relationship of peptides. For example, once the peptides
have been sequenced and their bioactivity has been determined
through in vitro and in vivo assays, they undergo structural prepa-
ration for docking. Next, the receptor-ligand complex structures
are prepared using docking simulation software. The final analysis is
done to predict the binding modes and affinities of a ligand, i.e.,
bioactive peptides [41].
3.2.1 Allergens The use of bioinformatics ranges from developing novel nutraceu-
ticals to detecting the toxic compounds in food, including aller-
gens. Regarding the detection of allergens, bioinformatics
facilitates the efficient detection of allergens from the massive
amount of data, predicting information about the allergen, and
can validate the traditional strategies by guaranteeing the reliability
of the conclusions. The bioinformatics approach can determine
cross-reactive allergens by determining the degree of homology of
different allergens within the epitome to maintain immunoglobulin
E (IgE) binding [49]. Bioinformatics was utilized in identifying
latent allergic proteins from chickpeas by collecting known allergen
sequences in the Fabaceae family from the database WHO/IUIS
(http://allergen.org) and Basic Local Alignment Search Tool
(BLAST). The study found that out of seven potential allergens
from chickpeas, four had cross-reactivity with the allergens in the
databases [50]. Another study utilized the proteomics and
METLIN database to identify hazardous allergens (glutaredoxin
and oleosin-B2) in bee pollen. Bee pollen is utilized for its
Computational Approach and Its Application in the Nutraceutical Industry 459
3.2.2 Bioactive Peptides In silico approach, prior to wet laboratory analysis, hydrolysis of
proteins allows focusing on a small number of peptides for predict-
ing the types and potency of peptides with the selected combination
of protein and enzyme(s) [52]. Bioinformatic approaches narrow
down the number of enzyme combinations for protein hydrolysis
and predict bioactivity or interaction with specific molecules and
receptors by homology-based searches [53]. The co-ordinate of the
cleavage point in the sequence could be based on the specialized
databases such as UniProt Knowledgebase [52]. Furthermore, with
the large set of databases, it is feasible to characterize peptides for
their theoretical physicochemical, specific bioactivity, and sensory
properties [54], and reject peptides with undesirable properties.
For example, Panjaitan, Gomez [55] did a study on optimiza-
tion of enzyme combination using in silico in order to render
tryptic peptides and determined their bioactive property. The resul-
tant peptides sequence was identified using mass spectrometry and
a sequence similarity search was done with BLAST, which revealed
that the aligned with tryptic peptide sequences from Epinephelus
coioides sharing 70% identity to the protein sequences from Epine-
phelus lanceolatus (database). Further, the BIOPEP analysis
revealed that the pepsin and mixed proteases (pepsin, trypsin, and
chymotrypsin A; pepsin, trypsin, and chymotrypsin C) exhibited
better production of ACEI peptides compared to other proteases.
In this way, the computational method is convenient for biotech-
nologists as it can efficiently identify peptide types and determine
appropriate protease combinations that can theoretically produce
optimal bioactive peptides.
3.2.3 By-products The utilization of food by-products is another growing field in the
food industry, which is blooming due to the development of bioin-
formatics tools. The combined application of in silico and ex vivo
has demonstrated the potential bioactivity (ACE inhibition, renin
inhibition, ACE inhibition,) of the peptides from by-products like
pigeon peas waste [56]. Senadheera et al. did a study on sea cucum-
ber where they utilized in silico techniques for generating antioxi-
dant and ACEI peptides by processing the by-products of sea
cucumber. The study utilized mass spectrometry to identified pep-
tides and was virtually screened by the PepRank tool. Then, in
silico, proteolysis was simulated with digestive enzymes using the
BIOPEP-UWMTM database tool. After simulated digestion, Tox-
inPred software evaluated the peptides for toxicity and found that
peptides resistant to the in silico digestion were non-toxic [57].
460 Prabina Bhattarai et al.
4.2 Artificial Neural Deep learning is a subset of machine learning that depends on a
Network (ANNs) and common algorithm with the important function of automatic
Deep Learning information extraction from raw data. Deep learning is a data-
hungry algorithm, and supervised learning datasets require a large
amount of labeled data. The use of more complex network archi-
tectures in DL expands on the use of deep artificial neural networks
(ANN) in ML. It utilizes the deep ANN made up of several layers of
nonlinear modules to enhance multilayer representation
[71]. Deep learning algorithms perform with accuracy and preci-
sion in ADMET property prediction, target prediction, virtual
screening, and chemical synthesis. Deep learning has been used
for high-performance test screening (HTS), quantitative structural
analysis (QSR), and other purposes. In recent years, de novo
Computational Approach and Its Application in the Nutraceutical Industry 463
5 Future Perspectives
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INDEX
Tanmay Sarkar and Siddhartha Pati (eds.), Bioactive Extraction and Application in Food and Nutraceutical Industries,
Methods and Protocols in Food Science , https://doi.org/10.1007/978-1-0716-3601-5,
© The Editor(s) (if applicable) and The Author(s), under exclusive license to Springer Science+Business Media, LLC, part of Springer
Nature 2024
469
BIOACTIVE EXTRACTION AND APPLICATION IN FOOD AND NUTRACEUTICAL INDUSTRIES
470 Index
C 300, 304, 311, 336, 340, 341, 343, 344, 347,
349, 358, 374, 420, 453, 456
Carbon ...................................................... 7, 8, 10, 31, 49, Distribution .....................................................25, 81, 144,
50, 95, 130, 132, 144, 156, 160, 161, 163, 164, 154, 166, 167, 169, 183, 209–211, 258, 263,
166, 236, 243, 264, 265, 279, 283, 287, 289, 300, 400, 451
316, 317, 321, 322, 360, 380, 381, 394, 395, Drug ....................................... 7, 25, 32, 34, 55, 57, 106,
411, 421, 426, 428 119, 121, 145, 164, 174, 177–179, 195, 196,
Carotenoids ............................................ 2, 13–16, 34, 50, 217, 285, 312, 374, 451, 453, 454, 461
53, 57, 59, 62, 80, 86, 89, 96, 105, 106, 117, 118,
134, 140, 143, 144, 147, 167, 174, 175, 177, E
183, 185, 190, 194, 203, 213, 217, 233, 234,
237, 243, 256–260, 283, 289, 300, 302–304, Economy.........................................................12, 204, 325
306, 307, 310, 311, 316, 319, 321–323, 393, Edible................................................. 51, 53, 61, 69, 113,
406, 426, 452, 453 115, 119, 164, 288, 289, 299, 310, 334, 358–360
Catalysts ............................................................9, 164, 365 Efficiency .................................................. 3–9, 11, 25, 48,
Chain ......................................................9, 51, 52, 54, 57, 69, 80, 86, 87, 89–93, 95, 96, 105, 106, 120, 122,
92, 163, 232, 240, 257, 299, 310, 325, 350, 357, 130, 134–137, 141, 142, 160, 162, 176, 177,
358, 363–365, 407 182, 183, 185, 188, 190, 193, 203, 204, 216,
Channels ...................................................... 206, 277, 339 217, 224, 230, 231, 245, 258, 261, 265–267,
Chromatographic ..............................................12, 22, 26, 276, 278–280, 282, 291, 293, 314, 318, 320,
28, 29, 283, 396, 436 323, 359, 361, 382, 384, 396, 398–400, 403,
Circular ................................................................. 204, 344 408, 410, 421, 422, 424–427, 429, 430,
Coatings.........................14, 31, 147, 165, 292, 293, 344 435–437, 440, 460–462, 464, 465
Commercialization ............................................... 413, 440 Emerging ...................................................... 2, 5, 7, 9, 69,
Comparison ..........................................31, 49, 51, 91, 92, 147, 255, 258–260, 269, 284, 313–315,
105, 113, 131, 136–138, 144, 145, 160, 204, 318–325, 419, 441
212, 216, 282, 365, 382, 442 Emulsions ................................... 13–15, 65, 66, 167, 191
Compliance.................................................................... 425 Encapsulation .................................................13, 146, 147
Compounds ..........................................1, 21, 45, 79, 103, Entry .............................................................................. 343
129, 155, 173, 202, 223, 255, 276, 301, 337, Environmental............................................ 4, 6, 7, 13, 16,
374, 391, 424, 449 46, 91, 105, 129, 137, 138, 155–158, 163, 169,
Consumer .......................................... 1, 13, 34, 164, 204, 170, 184, 185, 189, 194, 204, 236, 261, 262,
218, 256, 259, 270, 423, 430, 443 278, 282–284, 300, 301, 304, 322, 335, 337,
Control ....................................................... 16, 33, 66–68, 343, 347, 366, 383, 392, 393, 410, 421, 422, 455
107, 110, 191, 218, 224, 226, 246, 257, 265, Enzyme ..................................................... 6, 9, 22, 32, 33,
280, 313, 316, 335, 336, 344, 345, 347, 353, 54, 60, 66, 117, 134, 135, 138, 139, 143, 147,
356, 357, 360, 366, 394, 397, 399–401, 404, 166, 174, 175, 177, 180, 182–191, 193–195,
405, 413, 420, 428, 430, 437, 443, 458 197, 203, 206, 218, 236, 239, 245, 246, 248,
Cost-effectiveness.................................... 5, 239, 313, 422 256, 266, 269, 270, 303, 304, 309, 312, 323,
324, 334, 337, 348–350, 355–358, 360, 364,
D 365, 422, 427, 430, 439, 440, 457, 459, 462
Evaluation................... 65, 182, 262, 263, 362, 462, 463
Deep eutectic solvent (DES) ...................... 137, 162, 402 Extraction ..................................................... 2, 22, 46, 79,
Delivery........................................... 13–14, 106, 399, 461 103, 129, 153, 174, 202, 224, 256, 275, 301,
Demand ..................................................5, 15, 16, 34, 36, 334, 375, 391, 421, 451
69, 79, 158, 175, 177, 182, 204, 218, 219, 224,
237, 242, 246, 255, 270, 337, 443 F
Design....................................................... 16, 89, 91, 170,
207–211, 227, 228, 277, 278, 282, 288, 293, Fatty ............................................. 7, 9, 14, 16, 25, 33–35,
394, 397, 399, 401, 406, 410–412, 429, 47–50, 52, 54, 60, 61, 66, 67, 97, 140, 143, 167,
432–434, 437, 439, 440, 444, 460, 463 177, 212, 238, 241, 242, 245, 248, 278, 291,
Disease .................................................... 2, 14, 16, 33–37, 303, 304, 309, 310, 324, 340, 358, 360,
45, 55, 59, 61–63, 106, 117, 174–176, 195, 196, 363–365, 397, 420, 423, 430, 440, 443
232, 242, 244, 246, 247, 255–257, 260, 263, Films ................................................. 14, 61, 69, 113, 181
BIOACTIVE EXTRACTION AND APPLICATION IN FOOD AND NUTRACEUTICAL INDUSTRIES
Index 471
Flavonoids .......................................................2, 9, 14, 25, 300, 303–313, 333–336, 348, 358, 360, 362,
33, 34, 45, 62, 83, 85, 94, 96, 105, 117, 118, 120, 363, 365, 366, 391, 420, 424, 426, 433, 449,
129, 138–141, 143, 145, 174, 175, 177, 180, 451, 452, 454, 456
185, 186, 193, 196, 212, 213, 215, 217, 234, High-performance liquid chromatography
236, 237, 244, 256, 257, 259, 260, 262, 263, (HPLC)........................................... 12, 26, 29, 38,
266, 268, 286, 288, 302–309, 312, 315, 316, 143, 145, 156, 262, 264, 265, 267, 277, 282, 436
319, 322, 338, 393, 397, 400, 426, 437, 444,
461–463 I
Fluid.............................................................. 7, 10, 11, 22,
Impact....................................................... 7, 8, 22, 24, 33,
50, 95, 104, 106, 111, 121–123, 129–147, 156, 34, 47–49, 55, 67, 87, 89, 91, 105, 134, 136, 144,
159–162, 169, 178, 182, 196, 203, 217, 226, 155–157, 162, 163, 167, 185–188, 202, 203,
228, 245, 265, 275, 276, 278, 282, 285–287,
208, 212, 218, 224, 229, 230, 235, 241, 246,
292–293, 301, 316, 318, 321, 322, 358, 377, 256, 257, 260, 282, 300, 301, 322, 338, 343,
380–383, 392–398, 400–402, 410, 421, 423, 346–348, 353, 360, 377, 392, 403, 410, 412,
426, 428, 429, 431, 442
421–423, 434, 436, 437, 440, 450, 452, 454
Food.............................................................. 2, 21, 50, 96, Innovation ................................................... 382, 423, 465
103, 146, 153, 173, 201, 223, 255, 278, 299, Interactions.............................................9, 11, 15, 57, 82,
336, 374, 391, 419, 449
87–89, 132, 136, 138, 145, 180, 185, 186, 229,
Footprint ....................................................................... 282 257, 261, 276, 335, 337, 340, 346, 347, 352,
Form ............................................................. 8, 16, 34, 36, 360, 365, 366, 383, 393, 396, 398, 403, 404,
48, 51, 56, 88, 91, 109, 123, 130, 139, 143, 161, 407, 427, 440, 444, 450, 451, 456–460, 462–465
163, 166, 168, 178, 180, 182, 185, 187, 189,
In vivo ........................................12, 28, 38, 57, 120, 121,
205, 209, 225, 231, 256, 265, 266, 271, 281, 143, 145, 262, 263, 457
289, 292, 309, 310, 334, 336, 351–353, 358,
362, 383, 396, 401, 460, 462 L
Formulation................................................ 13, 14, 26, 36,
38, 69, 79, 145, 259, 263, 304, 312, 324, 358 Labeling ..........................................................22, 461, 462
Fourier transform infrared spectroscopy Liquid ...................................................5, 31, 48, 81, 105,
(FTIR)............................... 12, 26, 30, 31, 93, 182 130, 154, 182, 201, 224, 261, 276, 304, 354,
Functional................................................. 1, 2, 13–16, 31, 373, 392, 427, 463
33–35, 45, 46, 51, 56, 61, 69, 105, 115, 119, 129, Literature ...................................................... 38, 118, 119,
130, 135, 144, 167, 181, 184, 188, 217, 219, 190, 319, 321, 325, 453
242, 246, 248, 257, 259, 260, 263, 264,
M
269–271, 301, 302, 304, 310, 324, 339, 343,
348, 351, 358, 360, 419, 443, 444, 449–451, Marine source.........................46, 47, 50–64, 68, 69, 423
460, 462, 464 Market.................................. 61, 117, 177, 182, 218, 393
Future ........................................ 16, 36–38, 69, 147, 163, Mass ............................................. 6–8, 11, 14, 29–32, 38,
169, 195, 196, 218–219, 264, 277, 325, 348, 47, 48, 81, 89, 91, 105, 108, 109, 111, 123,
356, 381, 439, 463–465 130–136, 139, 141, 143, 158, 185, 188, 202,
224, 226, 230, 232, 237, 261, 267, 270, 276,
G 279, 281, 282, 284, 288, 317–319, 322–324,
Gas chromatography (GC) ................................... 12, 108, 354, 360, 364, 379, 380, 382–384, 392, 393,
143, 275, 282, 284, 436 395–398, 402–404, 411, 428, 436, 459
Good manufacturing practice (GMP) ......................... 425 Mechanisms ..................................... 8, 33, 34, 36, 56, 57,
Green technology................................................ 105, 119, 59, 81–82, 86, 92, 93, 107–112, 155, 156, 162,
134, 137, 201–219, 255, 266, 321, 391, 392, 169, 170, 189, 191, 195, 205–207, 218, 219,
421, 442 227, 237, 242, 246, 269, 277–279, 293,
334–342, 344, 348, 380, 385, 396, 404–405,
H 407–409, 429, 442, 450, 455, 457, 458, 460, 461
Methods................................................2, 22, 46, 80, 104,
Health ....................................................... 1, 2, 13, 15, 16,
130, 153, 176, 202, 224, 256, 277, 301, 334,
24, 32–34, 38, 46, 50, 55, 60–63, 69, 105, 113,
375, 392, 421, 455
117, 145, 155, 156, 163, 185, 187, 189, 195,
219, 224, 236, 242, 246, 255–257, 259, 285,
BIOACTIVE EXTRACTION AND APPLICATION IN FOOD AND NUTRACEUTICAL INDUSTRIES
472 Index
Microbial ................................................54, 57, 140, 205, Polyphenols .....................................................2, 9, 13, 14,
206, 224, 236, 239–241, 259, 263, 265, 301, 16, 24, 25, 30, 49, 51, 80, 86–88, 94, 105, 115,
337, 339, 346–349, 360, 454 120, 137, 139–141, 143, 146, 155, 175, 177,
Microencapsulation .............................146, 147, 292, 293 183–188, 196, 197, 203, 207, 208, 212–215,
Microwave .................................................... 8, 22, 48, 49, 217, 231, 233, 235, 240, 242–244, 257, 258,
80–82, 86–93, 95, 96, 104, 122, 134, 138, 142, 261, 264, 268, 270, 282, 284, 286–288,
147, 179, 217, 256, 267, 268, 270, 315, 302–305, 307–309, 312, 315, 319, 322–324,
319–321, 323, 379, 380, 403–405, 413, 428, 393, 397, 400, 406, 426, 433
437, 442 Positioning .................................................................... 398
Prebiotics ............................................334, 348–350, 357,
N 358, 362, 363, 365, 366
Preservation .................................................. 67, 113, 117,
Nanoencapsulation.......................................146, 292–293
Nanoparticles....................................................36, 65, 283 137, 184, 203, 204, 206, 216, 224, 237, 239,
Novel ............................................. 6, 8, 9, 11, 22, 46, 50, 245, 259, 380, 421, 428
Pressurised liquid ..............................................10, 11, 28,
55, 92, 129–147, 174, 182, 194, 202–204, 218,
224, 232, 236, 245, 248, 255–270, 276, 282, 104, 217, 261, 264, 268, 275–293, 316, 318,
283, 287, 301, 310, 312, 313, 318, 324, 346, 323, 324, 395, 399, 429
Pressurized.................. 10, 131, 140, 318, 377, 394, 400
391–413, 423, 431, 437, 439, 443, 450, 451,
456–458, 462, 463 Prevention ..........................................16, 33–37, 59, 202,
Novel solvent........................................................ 153–170 246, 255, 256, 271, 311, 358
Nutraceutical ................................................ 9, 13, 15, 16, Probiotics.........................................................33, 68, 263,
334, 348–350, 357, 358, 362–366, 420, 424
21–38, 45–48, 50–69, 80, 88, 96, 117, 129–147,
153, 167, 169, 170, 176, 180, 181, 202–204, Processing ................................................... 3, 7, 9, 13, 14,
219, 225, 232, 237, 241–248, 259–265, 270, 46, 49, 50, 55, 80, 105, 113, 122, 166, 167, 183,
187, 190, 191, 202–210, 216, 218, 219, 223,
271, 288, 292, 304, 324, 325, 333–366,
373–385, 391–413, 419–445, 449–465 224, 228, 237, 239–241, 245, 246, 248, 260,
Nutritional .................................................... 1, 14, 15, 61, 264, 266, 269, 289, 299–304, 318, 321, 322,
325, 336, 340, 343, 359, 378, 382, 385, 395,
65–68, 173, 181, 217, 218, 223, 224, 231, 235,
237, 248, 256, 260, 261, 302, 310, 312, 324, 401, 403, 411, 413, 425, 428, 457, 459, 460, 464
348, 350, 358, 366, 420, 443, 444, 458 Product .................................................1, 22, 61, 79, 103,
142, 156, 173, 203, 225, 256, 278, 301, 335,
O 374, 391, 420, 451