Powdered Water Kefir: Effect of Spray Drying and Lyophilization On Physical, Physicochemical, and Microbiological Properties
Powdered Water Kefir: Effect of Spray Drying and Lyophilization On Physical, Physicochemical, and Microbiological Properties
Powdered Water Kefir: Effect of Spray Drying and Lyophilization On Physical, Physicochemical, and Microbiological Properties
PII: S2772-753X(24)00155-2
DOI: https://doi.org/10.1016/j.focha.2024.100759
Reference: FOCHA 100759
Please cite this article as: Klinger Vinı́cius de Almeida , Vanessa Cortina Zanetti ,
Callebe Camelo-Silva , Luan Amaral Alexandre , Alice Cristina da Silva , Silvani Verruck ,
LucianoLuciano José Quintão Teixeira , Powdered water kefir: effect of spray drying and lyophilization
on physical, physicochemical, and microbiological properties, Food Chemistry Advances (2024), doi:
https://doi.org/10.1016/j.focha.2024.100759
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Highlights
The ideal fermentation condition was using 5% grains, 10% sugar and 25°C.
Freeze-drying preserved microbial viability better than spray-drying.
Spray-dried kefir powders showed better solubility compared to lyophilized
powders.
Zymomonas mobilis dominated kefir microbiota, constituting 94.31% of grains
2
Amaral Alexandreb, Alice Cristina da Silvab, Silvani Verruckb, Luciano José Quintão
Teixeiraa*
a
Departamento de Engenharia de Alimentos, Centro de Ciências Agrárias e
*Corresponding author:
Abstract
This study addresses the challenge of optimizing powdered water kefir's fermentation
technological characteristics. The main objective was to determine the best fermentation
conditions and evaluate the efficacy of different drying methods. The optimal
fermentation conditions were 5% kefir grains, 10% brown sugar, and an incubation
anomalus (grains: 3.00% and beverage: 26.77%) among fungi. The study innovatively
drying method. These methods retain the ideal physical-chemical properties and expand
the accessibility and practical applications of water kefir. This research underscores the
potential for powdered water kefir to deliver health benefits conveniently and
versatilely, paving the way for broader industrial and academic applications.
Abbreviations
4
MRS - De Man, Rogosa, and Sharpe Agar; DRBC - Dichloran Rose Bengal
Chloramphenicol Agar; PCA - Plate Count Agar; CFU - Colony Forming Units; FTIR
Deoxyribonucleic Acid; PCR - Polymerase Chain Reaction; V3/V4 - Third and Fourth
Variable Regions (of the 16S rRNA gene); w/v - Weight/Volume (percentage).
1. Introduction
food industry, aiming to meet the demand for healthier products (de Souza, Monteiro, et
al., 2024). Water kefir, a non-dairy kefir, is produced by fermenting water inoculated
with kefir grains in a sucrose solution. Brown sugar is typically used as the main
substrate for water kefir fermentation (Guzel-Seydim et al., 2021). However, various
vegetables and fruits, such as soy, onion, ginger, carrot, apple, pineapple, grape, quince,
kiwi, pear, melon, strawberry, pomegranate, tomato, and coconut, can also be used as
substrates. (Corona et al., 2016; da Silva Fernandes et al., 2017; Fiorda et al., 2017;
between 20 and 25 °C, after which fruit juices or pulps may be added to enhance flavor
(Laureys and De Vuyst, 2014). The resulting fermented beverage is carbonated, cloudy,
slightly alcoholic, and sweet, making it particularly popular among vegan consumers.
The grain cultivation conditions and microbiological composition largely determine the
beverage's composition (Fiorda et al., 2017). The final fermentation products include
5
ethanol, lactic acid, mannitol, acetic acid, glycerol, and other organic acids (Gulitz et al.,
2011).
varying microbial compositions in water kefir. Typically, water kefir grains comprise
lactic and acetic acid bacteria from genera such as Lactobacillus, Acetobacter, and
al., 2021; Xu et al., 2019). Traditionally, kefir microflora has been studied using
nutritional content of water kefir grains under different storage conditions (Gökırmaklı
networks during water kefir fermentation using non-targeted metabolomics (Ma et al.,
2024), functional quality of water kefir enriched with Haematococcus pluvialis biomass
and astaxanthin pigment (Yıldız et al., 2024), microbial composition of water kefir
grains and their application for detoxifying aflatoxin B1 (Ouyang et al., 2024), co-
mead (de Souza, Bogáz, et al., 2024) and the characterization of a product based on
quinoa extract fermented with water kefir grains (Sanches et al., 2024).
Despite the numerous studies associated with water kefir, several challenges
persist, including the lengthy production process, difficulty maintaining grain viability,
kefir could be a viable alternative to address these issues, offering longer shelf life,
easier storage, and instant reconstitution, making it a convenient product (Teijeiro et al.,
2018). On the other hand, to our knowledge, no prior study has focused on developing
powdered water kefir, making this research pioneering in describing the influence of
Spray drying and lyophilization are the most widely used methods for producing
powdered foods (Atalar and Dervisoglu, 2015; Chaturvedi et al., 2021). However,
various intrinsic and extrinsic parameters influence the overall powder formulation
process. These include the microorganisms' resistance to heat and cold, oxygen
specific drying agents like starches and maltodextrins are added, along with
(Chaturvedi et al., 2021). Trehalose and glucose form a glassy matrix and maintain
This study aims to develop and analyze powdered water kefir's physical,
2.1. Materials
7
The water kefir grains were acquired by donation from a local producer in the
Brazilian state of Santa Catarina. Water, brown sugar (Da Colônia, Santo Antônio da
Patrulha – RS, Brazil), inulin D.E. 10 (Beneo, Mannheim, Germany), and maltodextrin
D.E. 10 (Ingredion, Mogi Guaçu – SP, Brazil) were used in the production of water
Chloramphenicol Agar – DRBC (Merck, Germany), and Plate Count Agar – PCA
(Merck, Germany) were used for the microbiological assays. All reagents used were
analytical grade.
To maintain the viability of the kefir culture, the grains were inoculated and kept
in a solution of filtered water and brown sugar with soluble solids (SS) concentrations
(SolidSteel, Brazil). The grains were kept active and viable for fermentation with
continuous change of the nutrient solution every 24 hours, as described by Alves et al.
(2021).
In order to define the best fermentation parameters and subsequently submit the
To choose the best fermentation condition, the following parameters were used:
the condition with the highest lactic bacteria count, the condition with the highest grain
mass growth, and finally (according to Equation 1), the condition that at the end of the
48 hours of fermentation reached a pH of 4.5, considered optimal for water kefir (Fiorda
et al., 2017).
𝑚𝑘𝑓−𝑚𝑓𝑖
𝑋(𝑔⁄100 𝑔) = ( ) × 100 (Eq. 1)
𝑚𝑘𝑖
Where:
adjust mathematical models that describe the variation of the pH value as a function of
𝑛
^ = 𝑦𝑒𝑞 + (𝑦0 − 𝑦𝑒𝑞 )𝑒 −𝑘𝑡
𝑦 (Eq. 2)
Where:
𝑦
^: estimated value for the pH response variable
After defining the best fermentation condition, the microbial diversity of the
kefir grains and the fermented beverage was studied based on sequenced libraries using
the MiSeq Sequencing System equipment (Illumina Inc., USA) and the V2 kit, with 300
regions of the 16S rRNA gene and the ITS1 and ITS2 regions of the ITS intergenic
9
region, a 25 g/mL aliquot of the sample was homogenized with 225 mL of tryptone
saline. After this step, DNA extraction was performed using the magnetic bead
Technologies, Brazil. Then, the PCR reaction was performed in triplicate using
Platinum Taq Polymerase (Invitrogen, USA) under the conditions: 95 °C for 5 minutes,
final extension at 72°C for 2 minutes. The sequences were analyzed using a pipeline and
gene (Caporaso et al., 2012). For fungi, amplification was generated with primers for
sequences obtained were compared with proprietary or public databases (Quast et al.,
dehydrated. For spray drying and lyophilization, three formulations with different types
of carriers were developed to evaluate the effect on microbial viability and the effect of
the obtained powders on the physicochemical characteristics. The feed solution T01
consisted of using 20% (w/v) of maltodextrin as a carrier, feed solution T02 was
composed of 10% (w/v) maltodextrin and 10% (w/v) inulin, and finally, the T03 feed
10
solution had 20% (w/v) inulin as a carrier. The total solid contents were 17.65 ± 0.12
(T01), 17.44 ± 0.22 (T02), and 17.51 ± 0.22 (T03). The carriers were mixed with the
fermented beverage with a controllable speed homogenizer before and during drying.
dryer (B-290 mini spray dryer, Buchi, Flawil, Switzerland) at a constant inlet air
temperature of 135°C ± 1°C and a feed rate of 12 mL/min as per conditions described
by Atalar and Dervisoglu (2015) and Verruck et al. (2019), with adaptations. Under
2.4.2. Lyophilization
The different feed solutions (T01, T02, and T03) were frozen (-80 °C ± 2 for 24
same day they were produced. Then, the samples were lyophilized in a Liotop L101
lyophilizer (São Carlos, São Paulo, Brazil) and removed from the lyophilizer 24 h later
(pH, moisture, and water activity), physical (flow properties, hygroscopicity, solubility,
FTIR, DSC, color parameters, and particle morphology), and microbiological (lactic
The serial dilutions of the feed solutions and the powdered kefir samples were
carried out by transferring 1mL to 9 mL of 0.1% peptone water (w/v) with subsequent
11
inoculation in specific culture media. MRS agar was used to count lactic acid bacteria
(Merck, Germany), and the plates were incubated at 37°C under anaerobic conditions
for 72 h. DRBC agar was used to count molds and yeasts (Merck, Germany) with
incubation of the plates at 25°C for 24-72 h. For the identification of acetic bacteria,
Frateur agar (10 g/L yeast extract, 20 g/L Agar, 20 g/L calcium carbonate, and 20 g/L
ethanol) was used at an incubation temperature of 25°C for 5-10 days (Cassoni, 2008).
the electrode directly into the samples and into the powders in a 1% solution (Mettler
Toledo Seven Easy S20, Ohio, United States). Moisture was determined by direct
heating in an oven at 105°C. Water activity was determined using an Aqualab® 3TE
digital hygrometer (Decagon Devices Inc, Pullman, USA) at 25 °C. All analyses
The bulk (ρbulk) and tapped (ρtapped) densities were calculated as proposed by
Jinapong et al. (2008), with modifications. For bulk density calculation, 2 g of each
cylinders, and the filled volume was read. The same procedure was performed for
tapped density (ρtapped). However, before reading the volume, the test tube was tapped
vigorously against a surface until there was no further change in volume. Both the bulk
and tapped density were calculated by dividing the mass of the dry powder by the
powder sample to 25 mL of distilled and stirred water for 5 min using a magnetic stirrer.
The solution was centrifuged at 760 × g for 10 min, and 20 mL aliquot of the
oven at 105°C overnight, as described by Botrel et al. (2014). Water solubility (%) was
powder (1g).
FTIR using the Perkin Elmer Spectrum 100 spectrophotometer with a resolution of
4/cm in the region of 4,000–600/cm with the attenuated total reflection technique (ATR)
Shimadzu DSC-50 (Shimadzu, Kyoto, Japan). Approximately 5mg of each sample was
mL min−1 and heated from −30 °C to 210 °C, with a heating rate of 5 °C min−1. The
DSC device was preliminarily calibrated with an indium reference standard (Verruck et
al., 2018).
The color evaluation of the powders obtained was performed using a Byk
The total color difference (ΔE) between samples submitted to different methods was
2.12. Hygroscopicity
the method described by Dias et al. (2018). One gram of kefir powders was placed in
Petri dishes and then stored in a glass desiccator containing a saturated sodium chloride
JSM 6390 LV (Jeol, Tokyo, Japan), at an accelerating voltage of 10 kV. Samples were
fixed onto stubs and coated with gold using a cathodic vacuum atomization coater
the Statistica software version 13.3 (TIBCO Software Inc., Palo Alto, CA, USA) with
Table 1 shows the values obtained for the growth of lactic acid bacteria,
substrate consumption, and mass growth of water kefir grains in different fermentation
conditions. It was observed that the counts of lactic acid bacteria in the conditions
evaluated ranged from 5.42 0.08 to 6.71 0.19 log CFU/mL. The lowest counts of
this group of microorganisms were attributed to the T4 and T8 experiments, which may
be related to the percentage of kefir grains greater than the amount of substrate
available. Due to the dynamics of fermentation, the yeasts in the kefir grains hydrolyze
sucrose through the invertase enzyme, thus raising the levels of glucose and fructose in
the medium. Lactic acid bacteria can use these monosaccharides as a carbon source if
the medium favors their growth (Fiorda et al., 2017). The rapid consumption of sucrose
in the T4 and T8 tests, with values between 73.05 ± 0.03 and 72.71 ± 0.01%, suggests
that yeast metabolism has been favored. According to Magalhães et al. (2010), during
The tests with the highest lactic acid bacteria counts were the T1 and T3 tests,
with values of 6.50 and 6.71 log CFU/mL, respectively. Under these conditions, the
proportions of available sucrose were 1:1 and 2:1 (sucrose: grains). The greater
substrate available in the T3 test hypothetically did not cause disorder in the common
difference (p<0.05) was found in the average increase in the masses of the kefir grains,
which showed a growth ranging from 54.64 ± 1.47% to 100.86 ± 10.20% compared to
the initial masses of the grains during fermentation. The increase in grain mass occurs
during the backslopping process (inoculum reuse for the next fermentation) and is
(Laureys et al., 2019; Laureys and De Vuyst, 2017). The test with the highest grain
mass growth was the T3 test, in which substrate availability exceeds the number of kefir
grains inoculated. The same result was described by Laureys et al. (2018), in which the
Water kefir grain growth can slow down due to excess acid stress during
fermentation. Glucansucrases are enzymes lactic acid bacteria produce and are
responsible for water kefir grain growth. They are extracellular enzymes whose activity
is optimal at pH 4.0-5.5 and decreases at lower pH values (Côté and Skory, 2012;
Laureys et al., 2019; Waldherr et al., 2010). In this sense, the results shown in Figure 1
confirm that the T3 test at the end of 48 hours of fermentation presented the ideal pH
Figure 1 shows the pH variation curves for the different treatments and the
adjusted equations over time. The model proposed presented a good fit, i.e., good
agreement between the experimental values and the curve simulated by the model for all
(above 0.99). The evaluation of the pH value during fermentation proved to be a quick
and easy-to-obtain response, suitable for evaluating the fermentation process, regardless
Figure 1. Kinetics of pH variation for different water kefir fermentation conditions and
adjusted equations
17
T1: 5% kefir grains, 5% brown sugar, and incubation at 25°C; T2: 10% kefir grains, 10% brown sugar, and
incubation at 25°C; T3: 5% kefir grains, 10% brown sugar, and incubation at 25°C; T4: 10% kefir grains, 5% brown
sugar, and incubation at 25°C; T5: 5% kefir grains, 5% brown sugar, and incubation at 30°C; T6: 10% kefir grains,
10% brown sugar, and incubation at 30°C; T7: 5% kefir grains, 10% brown sugar, and incubation at 30°C; T8: 10%
kefir grains, 5% brown sugar, and incubation at 30°C.
18
According to Figure 1, the pH value of all evaluated conditions reduced over the
curve has a steeper slope between 5 and 15 hours of fermentation when the pH drops
more quickly. After this period, this slope becomes less pronounced, and the pH
decreases with less speed until it tends to remain in a range of very close values.
Experiments T5, T6, T7, and T8 that were incubated at 30°C showed the lowest pH
values at the end of 48 hours, all with values below 3.98 (Figure 1). Of these, the lowest
pH value observed was 3.94 for the T7 test. Velez and Peláez (2015) state that higher
amount of inoculum used. This author reports that in the proportions of 1:10 (grains:
milk), pH values between 3.6 and 3.8 were found, while in the proportions of 1:30 and
1:50 (grains: milk), pH values of 4.4 to 4.6 were found, respectively. The greater the
proportion of inoculated grains, the lower the pH values. This result corroborates the
values obtained in this study since the T4 and T8 experiments, which are the ones with
the highest proportion of grains inoculated 2:1 (grains: substrate), were the experiments
that presented the lowest pH values at their respective incubation temperatures (25 and
30°C). Zongo et al. (2020) in their study to evaluate beverages fermented by water kefir
grains, observed that the pH decreased from 6.53 to 4.07 after two days of fermentation
at room temperature (22ºC). The same authors state that the drop in the samples' pH
yeasts, which produce ethanol, volatile compounds, and carbon dioxide in addition to
producing acids.
acidity range of less than 4.5, the growth of the main microorganisms responsible for
19
foodborne illness is inhibited (Silva et al., 2018). Considering the value of 4.50 as the
optimal pH value for the completion of fermentation, we notice that the evaluated
experiments took different times to reach this value. At the end of the 48 hours of
fermentation, the predefined time for this study, the experiment that presented the
optimal pH value was the T3 experiment. This way, considering the pre-established
criteria for choosing the best fermentation condition, the T3 experiment with 5% grains,
10% sugar, and an incubation temperature of 25°C was considered the best condition to
fermented beverage, it was found that the bacterial compositions comprised nine genera
(Figure 2). Within these genera, nine distinct species were identified, and approximately
94.31% of the composition of the grains and 91.68% of the composition of the
high levels of ethanol, competing with the yeast Saccharomyces cerevisiae in terms of
yield, and are associated with traditional fermented beverages in tropical regions of
America, Africa, and Asia (Marsh et al., 2014; Weir, 2016). Patel et al. (2022) found
similar results in evaluating water kefir microbiota and flavor attributes. On the other
hand, Cao et al. (2019) conducted a study to evaluate the biodiversity of Chinese water
kefir grains. It showed a different result from this study because Z. mobilis was
responsible for only about 1% of the relative abundance. This variation may be related
to the natural selection that can occur over several generations for the same type of
20
Another species that appears in greater abundance when compared to the others
grains and 5.42% in the fermented beverage. This species has yet to be described in any
positive species isolated by Thamacharoensuk et al. (2015) from tree bark in Thailand.
in the grains and 0.62% in the fermented beverage). This species was also identified in
water kefir grains in the Brazilian states of Goiás, Bahia, and Distrito Federal (Miguel et
al., 2011), in water kefir grains obtained from different regions of Germany, and also
isolated from shochu (Gulitz et al., 2013), a traditional Japanese distillate made from
fermented rice, sweet potato, barley, and other starches (Endo and Okada, 2005). The
other species identified represent about 1.23% of the relative abundance in kefir grains
and 2.28% in the fermented beverage. Within these percentages are included in a
combined way (both grains and beverage) the genus Lactobacillus sp. (1.35%) and the
mesenteroides (0.19%).
21
Figure 2. Relative abundance (%) of bacteria (A) and fungi (B) species in water kefir
Fermented Beverage
Grain
A
0% 20% 40% 60% 80% 100%
Relative abundance of bacterial species (%)
Zymo monas mobilis Sporolactobacillus spathodeae Liquorilactobacillus satsumensis
Lactobacillus sp. Lentilactobacillus hilgardii Oenococcus kitaharae
Acetobacter peroxydans Gluconobacter frateurii Leuconostoc mesenteroides
Fermented Beverage
Grain
B
0% 20% 40% 60% 80% 100%
Relative abundance of fungal species (%)
Phaffomycetaceae were detected in the grains and fermented beverages. Five genera
were identified in the grains and fermented beverages (Figure 2). The species
67.53% of the composition of the fermented beverage (Figure 2B). For years, this
22
species has been associated with grape must and wine fermentation processes in several
wine-producing countries (Porter et al., 2019). Unlike what was obtained in this study,
Gulitz et al. (2011) and Cordeiro (2018) found lower relative abundances for the genus
L. fermentati. The percentage was 6-8% in fermented beverages based on water kefir
and 2.27% in kefir grains obtained from consumers in the Brazilian state of Paraná,
respectively.
anomalus, with 3.00% in the grain and 26.77% in the fermented beverage. W.
anomalus, formerly known as Hansenula anomala, occur naturally in grape must and
has been evaluated for enhancing the aroma of wines by producing volatile compounds
(Lombard, 2016). Laureys et al. (2017) also identified the species W. anomalus while
investigating water kefir grains' instability and low growth during an industrial
fermentation process. The same identification occurred in the study of isolation and
molecular identification of yeasts in kefir, albeit in milk kefir grains obtained through
Fungal species with lesser representation were also identified, such as the genus
Saccharomycetes sp. (0.66% in the grain and 0.60% in the fermented beverage) and the
species Saccharomyces cerevisiae (0.55% in the grain and 4.03% in the fermented
beverage), Torulaspora delbrueckii (0.14% in the grain and 0.33% in the fermented
beverage), and Candida californica (0.11% in the grain and 0.73% in the fermented
beverage).
Table 2 presents the results of microbial counts demonstrating the effect of the
three compositions of carrier materials and two drying methods for the powders
23
obtained from the best fermentation condition previously evaluated for water kefir. The
lactic acid bacteria counts in the different feed solutions did not differ significantly from
each other (p>0.05). When these solutions were subjected to spray drying, there was a
reduction (p<0.05) in the initial count. Thermal, osmotic, oxidative, and desiccation
stresses are generally considered the main mechanisms that cause bacterial inactivation
during and after spray drying (Arepally et al., 2020). Cellular damage caused by heat
action includes DNA and RNA denaturation, ribosomal damage, dehydration, and
plasma membrane destabilization due to water removal (Cebrián et al., 2017). Teijeiro
et al. (2018) reported that after spray drying, the viability of lactic acid bacteria in kefir
powder made with UHT milk was reduced by approximately 2.5 logs CFU/g.
Table 2. Microbial counts before and after spray drying and lyophilization
Lactic acid bacteria (log Molds and Yeasts (log Acetic acid bacteria (log
Test
CFU/g) CFU/g) CFU/g)
FST01 7.17 ± 0.43aA 5.14 ± 0.15aA 5.04 ± 0.22aA
FST02 7.07 ± 0.25aA 5.65 ± 0.42aA 5.25 ± 0.65aA
FST03 7.19 ± 0.55aA 5.53 ± 0.40aA 5.75 ± 0.37aA
T01S 3.76 ± 0.20aB 2.99 ± 0.21aB 2.38 ± 0.58aB
T02S 3.41 ± 0.48aB 3.03 ± 0.29aB 2.69 ± 0.53aB
T03S 3.85 ± 0.36aB 3.19 ± 0.43aB 2.92 ± 0.67aB
T01F 6.35 ± 0.18aA 5.03 ± 0.08aA 4.80 ± 0.02aA
T02F 6.75 ± 0.15aA 5.40 ± 0.01aA 4.46 ± 0.30aA
T03F 6.69 ± 0.83aA 5.41 ± 0.03aA 4.66 ± 0.26aA
Results are expressed as mean ± standard deviation (n = 2). Different lowercase letters between lines show a
significant difference (p<0.05) among the evaluated tests. Different capital letters between lines are significantly
different (p<0.05) between the drying processes used. FS – Feed solution before the drying process; T01S – test using
100% maltodextrin as dry carrier in spray dryer; T02S – test using 50% maltodextrin and 50% inulin as dry carriers
in spray dryer; T03S – test using 100% inulin as dry carrier in spray dryer; T01F – test using 100% maltodextrin as
dry carrier by lyophilization; T02F – test using 50% maltodextrin and 50% inulin as dry carriers by lyophilization;
T03F – test using 100% inulin as lyophilized carrier.
No differences were shown (p>0.05) for the mold and yeast counts in the
different feed solutions. This result corroborates the one obtained by Rodríguez et al.
(2023), who found yeast counts close to 5.30 logs CFU/g, and with the study of
Villanoeva et al. (2021), who reported a value of 5.89 to 6.86 log CFU/g of yeasts for
water kefir. In optimizing spray drying parameters of kefir powder, Atalar and
24
Dervisoglu (2015) found yeast counts in the 4.54–5.89 logs CFU/mL range. In our
study, spray drying promoted a logarithmic reduction (p<0.05) of 2.15, 2.62, and 2.34
for T01, T02, and T03, respectively. This result demonstrates that spray drying failed to
maintain the viability of molds and yeasts. The low thermotolerance of yeasts has been
al., 2021). When the feed solutions were subjected to the lyophilization process, no
In this sense, lyophilization emerges as the best drying technique for water kefir, which
aligns with the conclusions obtained in investigations focused on drying milk kefir
Similar behavior was observed regarding acetic bacteria when the T01, T02, and
T03 were submitted to the drying processes. Thus, there was a reduction in the initial
viability for tests dried in a spray dryer and maintenance of viability for tests submitted
to lyophilization (Table 1). Tontul et al. (2021) obtained similar results; however, they
informed that it is difficult to obtain linearity of the results since there are differences in
is being evaluated. Usually, the carriers help maintain the viability of microorganisms
(Coutinho Favilla et al., 2022; Teijeiro et al., 2018). Within the scope of this research,
the evaluated wall materials (maltodextrin and inulin) showed the same performance. In
this way, choosing any carrier tested for drying water kefir becomes possible. Another
point observed is that the spray dryer parameters used in this study, according to the
optimization performed by Atalar and Dervisoglu (2015), were not ideal, considering
the evaluated microorganisms' viability loss. There are many manners to optimize the
drying process using a spray dryer. In addition to using carriers and changing the inlet
25
temperature, adaptations can be made to the spray dryer equipment, such as Tabatabaei
et al. (2022), which utilized a spray dryer equipped with an electrostatic collector to dry
chitosan. This new technology can be used in future studies to verify the protective
different carriers can vary according to the methods used in production and can impact
properties evaluated.
The lowest (p<0.05) pH value was attributed to T01 considering spray drying,
while for lyophilization, the sample that presented the highest (p<0.05) value was T03.
When comparing the drying methods, the samples submitted to the lyophilization
process showed higher pH values (p<0.05) than those submitted to spray drying. During
lyophilization, as water is removed from the material, the concentration of ions in the
Results are expressed as mean ± standard deviation (n = 3). Different lowercase letters between lines show a
significant difference (p<0.05) between the different wall materials. Values followed by different capital letters
between columns differ significantly (p<0.05) between drying processes. T01 – test using 100% maltodextrin as the
carrier; T02 – test using 50% maltodextrin and 50% inulin as the carrier; T03 – test using 100% inulin as the carrier.
L* indicates the lightness, a* the variation from red (+a*) to green (–a*), b* the variation from yellow (+b*) to blue
(–b*), and ΔE total color difference.
The food industry knows that powdered products' ideal moisture content should
be between 4 and 7% so that they are stable during storage (Teijeiro et al., 2018). Thus,
all powders obtained meet this premise and are considered stable products. In addition,
which is one of the quality parameters for powders containing viable microorganisms
Water activity (aw) is related to the availability of free water in the sample and is
also an important parameter that determines powders' stability and shelf life during
storage (Wang et al., 2020). In the present study, aw showed behavior similar to the
moisture analysis results. According to Tapia et al. (2020), water activity values
between 0.20 and 0.40 guarantee the stability of the stored product against browning
27
Therefore, all the powders obtained in the present study are within the range considered
Powdered foods with less than 10% hygroscopicity are classified as non-
hygroscopic (Costa et al., 2014). Therefore, the kefir powders in the present study
obtained through spray drying and lyophilization are classified as hygroscopic with
special packaging. The powder produced only with maltodextrin (T01) was the powder
with the lowest (p<0.05) hygroscopic nature for both drying processes. As the addition
of inulin was performed as wall material in T02 and T03, an increase in hygroscopicity
was observed. This behavior differs from what Mensink et al. (2015) expect. According
to the authors, inulin is a material with a higher degree of polymerization, has fewer
reducing groups, has a higher glass transition temperature, and, therefore, has a lower
desirable (Bicudo et al., 2015). Different factors such as the chemical composition of
size, porosity, shape, and others), and wall materials (if any) affect the solubility of
powdered food (Tontul and Topuz, 2017). In the present study, the type of wall material
used had no significant effect on powder solubility, while the drying method applied
had a significant influence (p<0.05). The tests submitted to the spray drying process
showed solubility greater (p<0.05) than the solubility of the lyophilized samples. The
higher solubility of the samples submitted to the spray drying process may be due to the
smaller particle size obtained for these samples since the smaller the particle size, the
greater the surface area available for hydration (Kuck and Noreña, 2016).
28
as density is essential because they inherently affect the behavior of the powder during
Regarding density, it was observed that the carrier agents employed influenced and
caused differences between the values obtained for the tapped and bulk densities of the
powders. T03 subjected to spray drying and lyophilization for bulk density showed
higher values (p<0.05) than the others. Lower bulk densities result in a larger package
volume; therefore, they are undesired. On the other hand, high bulk densities increase
powder stability and improve protection against oxidation (Himmetagaoglu and Erbay,
2019).
Furthermore, it was observed that the tapped density of the powders tended to
increase as inulin was added to the feed solution as wall material. That way, the
powders obtained for T02 and T03 through spray drying and lyophilization were equal
(p>0.05) to each other and greater than those obtained in test T01 with 100%
maltodextrin as a carrier agent. Regardless, when comparing the drying methods, the
powders obtained by lyophilization showed lower (p<0.05) tapped density than spray
drying. The lower tapped density of samples produced by lyophilization may be related
to the more porous structure caused by the drying method, thus causing a high volume
For the color parameters, despite varying (p<0.05) between the drying methods,
it is noted that all powders had high L* values, which indicates a light color with a
coloration, while the b* parameter suggests a yellowish color, which can be attributed to
the brown sugar in the test formulation. No difference (p>0.05) was observed between
the drying methods used for the parameter a*, suggesting that this parameter low
29
influences the color of the sample differences observed in ΔE*. Thus, Martínez-
Cervera et al. (2011) report that the human eye cannot visually perceive total color
difference (ΔE*) values smaller than 3. Thus, it was possible to verify that all evaluated
samples were affected by the drying methods, suggesting a significant change in color
acceptability, ensuring that color variations do not compromise the sensory experience
or consumer acceptance.
FTIR analysis can be applied to investigate the chemical and structural changes
that occur during spray drying and lyophilization of water kefir, using different carriers,
such as inulin, maltodextrin, and the mixture of the two materials. Figure 3 (I) shows
the FTIR spectra for spray-dried and lyophilized kefir powders. When analyzing the
spectra, the most significant absorption bands, which provide more information about
samples, range from 3409 to 2889/cm and from 1647 to 930/cm (fingerprint region). It
bonds in carbohydrate molecules, such as maltodextrin and inulin (Barbosa, 2013; Paiva
et al., 2013). At 2925 and 2893/cm, two bands of medium intensity are observed,
referring to asymmetric and symmetric stretching of C-H bonds of sp³ carbons (Barbosa,
2013; Paiva et al., 2013). In addition to these bands, there is also a band at 1648/cm,
which is related to the stretching of the C=O bond of carboxylic acids and esters,
possibly formed in fermentation processes (Paiva et al., 2013; Romano et al., 2018).
Finally, at 1080, 1028, 999, and 930/cm, intense bands are observed inherent to the
stretching of ether groups present in carbohydrates and of the O-C-O glycosidic bonds
30
of saccharides, such as maltodextrin and inulin (Barbosa, 2013; Paiva et al., 2013;
Romano et al., 2018). These observations indicate that the carriers used (inulin,
maltodextrin, and their mixture) do not significantly alter the fundamental chemical
characteristic absorption bands across all samples. The data suggest that both spray
drying and lyophilization processes maintain the integrity of the kefir's key chemical
microscopy (SEM), and thermograms (III) of spray-dried and lyophilized water kefir
powders
T01S – test using 100% maltodextrin as carrier in spray dryer; T02S – test using 50% maltodextrin and 50% inulin as
carriers in spray dryer; T03S – test using 100% inulin as carrier in spray dryer; T01F – test using 100% maltodextrin
as carrier in lyophilization; T02F – test using 50% maltodextrin and 50% inulin as carriers in lyophilization; T03F –
test using 100% inulin as carrier in lyophilization. A, B, and C: spray-dried kefir particles using 100% maltodextrin,
50% maltodextrin, and 50% inulin; and 100% inulin, respectively; D, E, and F: lyophilized kefir particles using 100%
maltodextrin, 50% maltodextrin, and 50% inulin; and 100% inulin, respectively.
– SEM of the kefir powder particles produced using different carrier agents and drying
porous, irregularly shaped, and disordered. Ice crystals form due to the low
temperatures and sublimate under reduced pressure, forming dry and porous products
(Dolly et al., 2011). Cavalcante (2016) observed similar morphology in soursop pulp
particles obtained through lyophilization. Caparino et al. (2012) also observed porous
surfaces when analyzing microscopic images of powdered mango pulp obtained through
lyophilization. On the other hand, the spray-dried kefir microparticles showed different
For the sample produced using maltodextrin as wall material (Fig. 3 (II) A), the
microcapsules were spherical, smooth surfaces and without cracks or pores. As inulin
was incorporated into the samples as a wall material, the microcapsules showed ovoid
morphology and apparent roughness (Fig. 3 (II) B and C). Another point observed is
that with the inclusion of inulin in the samples, the particles increased in size, as shown
in the images (Fig. 3 (II) B and C). This increase corroborates the previously mentioned
density values since, as inulin was included as a carrier agent, the values of tapped and
bulk densities also increased. Silva (2021) found similar behavior when maltodextrin,
inulin, and the combination of both were evaluated as carrier agents in the drying
DSC analysis can be applied to investigate the thermal changes in water kefir
during spray drying and lyophilization using different carriers, such as inulin,
maltodextrin, and a mixture of the two materials. The DSC curves of the evaluated
samples are shown in Figure 3 (III). The curve belonging to the fermented beverage
showed some distinct endothermic events between 65 and 200 °C. For this event, the
the water present in the beverage formulation. Another observed peak occurred at a
temperature of 179.75°C (ΔH = 24.0024 J/g), which may be associated with the melting
beverage's fermentation. In the literature, there are quite variable melting temperature
records for sucrose with values of 165, 176, 185.9, 184.1, and 192 °C (Maia, 2019;
The DSC curves of the spray-dried kefir powders showed a well-defined thermal
event at temperatures of 190.65, 195.15, and 198.82 °C relative to tests T01S, T02S,
and T03S, respectively. The endothermic peaks observed in the tests are related to the
loss of hydrophilic groups present in the sample's characteristic of their melting point.
The calculated enthalpy of fusion (ΔH) was 43.9302, 26.0924, and 1.2326 J/g relative to
tests T01S, T02S, and T03S, respectively. For the samples obtained by the
temperatures of 194.73, 176.56, and 200.46 °C (ΔH = 11.5670, 3.1191, and 1.6036 J/g)
The endothermic peaks observed in the T01S and T01F tests (194.65 and 194.73
°C) that contain maltodextrin as a carrier suggest a better efficiency in the encapsulation
process when compared to the other tests. This hypothesis can be inferred from the
difference in values of the characteristic endothermic peaks at the melting point of the
33
tests mentioned and pure maltodextrin (241.05 °C; ΔH = 95.9417 J/g). According to
Maia (2019), when microcapsule formation does not occur, the endo and exothermic
It is also verified that as inulin is added as a carrier in the T02S, T03S, T02F,
and T03F tests, there is an increase in the endothermic temperature when compared to
the T01S and T01F tests in which 100% maltodextrin was used as a carrier. This
behavior suggests a lower efficiency in the encapsulation process since the peak
temperatures of the T02S, T03S, T02F, and T03F tests are close to — or at least
approaching — the temperature characteristic of the inulin melting process (203.48 °C;
ΔH = 28.2166 J/g). Based on these results, it can be stated that the microencapsulation
towards stability of the powders obtained compared to the tests using inulin as a carrier.
The physical and physicochemical properties evaluated revealed that water kefir
fermentation conditions were achieved using 5% water kefir grains, 10% sugar, and an
probiotics and viable microorganisms, drying kefir by lyophilization was the best
method for producing stable food with preserved viability of the microorganisms
Based on the results obtained, some directions for future research on powdered
water kefir can be recommended. Firstly, evaluating the effects of more different types
impacts water kefir's functional and bioactive properties, including its antioxidant and
life of water kefir powders and identifying key factors that affect their longevity would
formulations from water kefir powders and assessing their sensory acceptance and
consumer purchase intent could enhance product development. Another promising area
water kefir fermentation and their effects on gut microbiota modulation. Finally,
conducting in vivo studies in animals and humans to evaluate the health benefits of
regular water kefir consumption, such as improved immune function and reduced
inflammatory markers, would further substantiate the positive impacts of water kefir on
health.
Writing – original draft. Vanessa Cortina Zanetti: Formal analysis, Data curation.
Callebe Camelo Silva: Formal analysis, Data curation. Luan Alexandre Amaral:
The authors declare that they have no known competing financial interests or
personal relationships that could have appeared to influence the work reported in this
paper.
Acknowledgments
The authors would like to thank CNPq (National Council for Scientific and
the Foundation for Research Support of Santa Catarina - FAPESC [grants number
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Declaration of interests
☒ The authors declare that they have no known competing financial interests or
personal relationships that could have appeared to influence the work reported in this
paper.
☐The authors declare the following financial interests/personal relationships which may be
considered as potential competing interests:
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Graphical abstract