Bioprocess Biosyst Eng
DOI 10.1007/s00449-017-1851-6
RESEARCH PAPER
A simple and efficient method for the extraction and separation
of menaquinone homologs from wet biomass of Flavobacterium
Hongfei Wei1,2 · Genhai Zhao1 · Hui Liu1 · Han Wang1,2 · Wenfeng Ni1,2 ·
Peng Wang1 · Zhiming Zheng1
Received: 24 May 2017 / Accepted: 4 October 2017
© Springer-Verlag GmbH Germany 2017
Abstract Menaquinone homologs (MK-n), that is, MK-4,
MK-5, and MK-6, can be produced by the fermentation of
Flavobacterium. In this study, we proposed a simple and efficient method for the extraction of menaquinones from wet
cells without the process of drying the biomass. Meanwhile,
a rapid and effective solution for the separation of menaquinone homologs was developed using a single organic solvent, which was conducive to the recovery of the solvent.
The results showed that the highest yield was obtained with
pretreatment using absolute ethanol at a ratio of 6:1 (v/m)
for 30 min and then two extractions of 30 min each using
methanol at a ratio of 6:1 (v/m). The recovery efficiency of
the menaquinones reached to 102.8% compared to the positive control. The menaquinone homologs were effectively
separated using methanol as eluent at a flow rate of 0.52 mL/
min by a glass reverse-phase C18 silica gel column with a
height-to-diameter ratio of 5.5:1. The recovery of menaquinones achieved was 99.6%. In conclusion, the methods for
extraction and separation of menaquinone homologs from
wet Flavobacterium cells were simple and efficient, which
makes them suitable not only on a laboratory scale but also
for application on a large scale.
* Peng Wang
pengwang@ipp.ac.cn
* Zhiming Zheng
zhengzhiming2014@163.com
1
Key Laboratory of Ion Beam Bioengineering, Hefei
Institutes of Physical Science, Chinese Academy
of Sciences, Hefei 230031, People’s Republic of China
2
University of Science and Technology of China,
Hefei 230026, People’s Republic of China
Keywords Wet cell extraction · Separation ·
Menaquinone homologs · Flavobacterium
Introduction
Menaquinone (MK)-n refer to a series of naphthoquinone
derivatives, where n denotes the number of isoprene units in
the side chain. It is generally presumed that menaquinones
are produced during the fermentation of bacteria such as
Escherichia coli, Flavobacterium, Deinococci, and Bacillus subtilis natto [1, 2]. The previous studies have shown
that menaquinones are more effective clinically than phylloquinone with respect to osteoclastogenesis, hypocholesterolemic effects, and ability to slow atherosclerotic progression [3]. Bioassay data suggested that menaquinones as
compared to phylloquinone were more efficient in reversing
vitamin K deficiency, which, indeed, is due to their longer
duration of biological response and slower hepatic turnover
[4, 5]. However, these valuable compounds are not readily
available at an affordable price, because their production
involves several tedious and inefficient unit operations [6].
The extraction of menaquinones from the fermentation
medium plays a critical role. Apart from the fermentation
conditions, low extraction efficiency results in product loss
and time consumption,even when high concentrations are
achieved in the fermentation medium. Menaquinones are
commonly recovered from microbial cells by a solid-phase
extraction technique [7, 8], liquid–liquid extraction technique [2, 6, 9, 10], or supercritical fluid extraction technique [11–13]. However, all of these extraction methods are
associated with some disadvantages as they involve complex
procedures such as time-consuming sample pretreatment in
the drying step and different organic solution proportions
or expensive devices and high energy input. Therefore, it
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Bioprocess Biosyst Eng
is necessary to develop a rapid and efficient method for the
extraction of menaquinones from fermentation media.
The characteristics of the side chain have a significant
impact on the lipophilicity of a vitamer and may also result
in substantial differences in properties such as intestinal
absorption, transport, tissue distribution, and bioavailability [14]. There are several studies that correlate a high concentration of MK-4 with the levels of sphingomyelin and
sulfatides in the brain, suggesting its role in the biosynthesis
of this important class of lipids [15, 16]. On the other hand,
some studies suggest that the bioavailability of menaquinone is related to the length of the side chain, such that
medium-length menaquinones are more bioavailable than
short-chain ones [17]. Obviously, menaquinones with side
chains of different lengths could have different functions in
the body. Therefore, it is necessary to separate the menaquinone homologues so as to match the remedy to the case and
improve the efficiency of menaquinones.
The present study proposed a rapid and effective method
for the extraction of menaquinones from wet biomass of
Flavobacterium fermentation, in which the time and energy
consumed in drying the cells was omitted. We designed different experimental conditions that involved varying the
solvent, processing time, and water percentage of the wet
microbes for optimization purposes. Meanwhile, we developed a simple method for separating menaquinone homologues produced by Flavobacterium using a single organic
solvent. Several separation conditions, including the choice
of organic solvent, flow rate, height-to-diameter ratio, recovery ratio, and loading quantity of the menaquinones were
evaluated to optimize the process.
Materials and methods
Reagents and standards
Chromatographic quality methanol and dichloromethane
obtained from Sigma–Aldrich (USA) were used as eluents in
the mobile phase of HPLC. All other chemicals and organic
solvents purchased from Sinopharm Chemical Reagent Co.
Ltd. (China) were used to extract menaquinones from wet
microbes and for the culture substrate. The menaquinone
standard, MK-4, was purchased from Sigma-Aldrich (USA).
The stock solutions were individually prepared in methanol
(Sigma) and protected from light exposure and evaporation
during storage.
HPLC conditions and statistical analysis
The extracted menaquinones were analyzed with an LC-16
HPLC system (Shimadzu, Kyoto, Japan) equipped with a
UV–Vis detector (SPD-16, Shimadzu) and column oven
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(CTO-16, Shimadzu). The analytical column was a reversephase C18 (VP-ODS, 4.6 mm I.D. × 250 mm, Shimadzu),
and the temperature of the column was maintained at 35 °C.
The UV–Vis detector was operated at 248 nm for menaquinones. A mixture of methanol and dichloromethane (4:1,
v/v) was used as the mobile phase at a flow rate of 1.0 mL/
min. Aliquots of 20 μL were injected manually using a loop
injection valve (Shimadzu). Menaquinone species were
identified and quantified according to their retention times
and the UV spectrum of each peak was observed in UV
detector. Menaquinone-4 (MK-4) was used as the quantitative standard for the menaquinones. The amounts of
menaquinones were calculated from the peak areas based
on the standard curves of MK-4. All extraction experiments
were repeated at least three times and the data were analyzed
for comparison by the software SPSS 19 and reported as
mean ± standard deviation (SD). The yield was expressed
as mg menaquinones/g dry biomass.
Cell cultures and harvesting
The media consisted of 2% glycerol, 1% peptone (fish),
0.15% yeast extract, 0.45% K2HPO4, 0.3% NaCl, and 0.03%
MgSO4·7H2O were inoculated with 10% Flavobacterium
seed solution. Fermentation was conducted for 6 days aerobically at 37 °C and 200 rpm in a rotary shaker in a 30-L
fermenter containing 18 L of identical media.
Sample preparation
At the end of cultivation, the cells in 25 mL of fermentation
liquor were placed in a 50-mL centrifuge tube and centrifuged at 12,000 rpm for 15 min. The weight of the isolated
wet cells was calculated as: wet cells weight (WCW) = total
weight of the centrifuge tube containing wet cells − weight
of the empty centrifuge tube. A few of the tubes containing wet cells were lyophilized for 24 h. And then, the
weight of the dry cells was calculated as: dry cells weight
(DCW) = total weight of the centrifuge tube containing dry
cells − weight of the empty centrifuge tube. The water content in the cells was calculated from the following formula:
water content = (WCW − DCW)/WCW × 100%.
Extraction of menaquinones from dry cells
The dry samples were crushed and then treated according to the following procedures: Various organic solvents,
including methanol, absolute ethyl alcohol, acetone,
n-butanol, trichloromethane, isopropyl alcohol, acetonitrile, n-hexane, and petroleum ether were individually
added to the centrifuge tubes at a ratio of 10:1 (v:m) and
mixed with the bacterial sludge followed by quiescent
extraction for 1 h. Then, the samples were centrifuged at
Bioprocess Biosyst Eng
12,000 rpm for 10 min and each supernatant was collected
as the first extraction solution. The foregoing extraction steps were repeated twice, and the second and third
extraction solutions were collected. All extractions were
conducted at room temperature. The volume of the three
extracts supernatant was quantified, and the content of
menaquinones was measured and calculated with HPLC
for future analysis. The organic solvent that gave the maximum extraction yield of menaquinones from the dry cells
was designated as the positive control.
Extraction of menaquinones from wet microbes
The extraction procedure from the wet microbes was the
same as that from the dry cells except for the sample pretreatment by lyophilization. The organic solvent that gave
the maximum extraction yield of menaquinones from the
wet cells was designated as the negative control.
Improved extraction procedures for wet cells
An appropriate volume of absolute ethyl alcohol was added
to the wet microbes contained in the centrifuge tubes, so
that the ratio of the volume of ethanol to the weight of wet
cells was ranged from 2:1 to 7:1 (v:m). At the same time, an
appropriate volume of methanol was added to the positive
control (dry cells) and negative control (wet cells) at a ratio
of 6:1 (v:m). And then, the samples were mixed, followed
by quiescent extraction for 1 h. Each supernatant was collected as the first extraction solution after centrifuging at
12,000 rpm for 10 min. The same proportion of methanol
as used for the first extraction of the controls was added to
the samples and controls, mixed, and extracted quiescently
for 1 h. After centrifugation, the supernatants were designated the second extracts. This step was repeated once to
obtain a set of third extracts. The three supernatant of each
sample were quantified with HPLC and the total content of
menaquinones was calculated. All samples were conducted
in triplicate.
Separation of menaquinone homologs
The extracts of menaquinones were evaporated to dryness
under reduced pressure and re-dissolved in a single organic
solvent such as methanol, absolute ethyl alcohol, or acetonitrile. A glass column filled with reverse-phase C18 silica gel
was made up according to the manufacturer’s instructions.
Different organic solvents were added to elute the menaquinones. The flow rates, height-to-diameter ratios, and recovery ratios of the menaquinones were evaluated for optimization purposes. The menaquinone homologs were determined
by their absorptions and mass spectra with an LC–MS system equipped with a 6200 series TOF/6500 series analyzer
(Agilent Technologies, Santa Clara, CA, USA).
Results
Effect of extractions of menaquinones from dried
and wet microbes
The extractions of menaquinones from dry Flavobacterium
cells were initially carried out using different organic solvents at room temperature without any modifier, and the
extraction yields are shown in Fig. 1. Obviously, the extraction yields obtained by using methanol, absolute ethyl alcohol, acetic acid, and n-butanol were higher than those of the
other solvents. The highest extraction yield was obtained
using methanol (P < 0.05) and was set as the positive control
in the following experiments.
The extraction yields of menaquinones from wet microbes
using different organic solvents are shown in Fig. 2. The
Optimization of pretreatment time for the wet biomass
The optimal ratios of absolute ethyl alcohol and methanol
to wet cells were used for extractions. Firsts, the samples in
centrifuge tubes were pretreated with ethanol quiescently
for 10, 20, 30, or 40 min, and then, they were extracted with
methanol twice for 30 min each time. The three supernatant
of each sample were quantified with HPLC and the total
contents of menaquinones were calculated. All samples were
conducted in triplicate.
Fig. 1 Concentration of menaquinones obtained from dry cells using
different extractants. Extraction was carried out three times with
5 mL of organic solvent for 1 h each time at room temperature
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Bioprocess Biosyst Eng
Fig. 2 Concentration of menaquinones obtained from wet cells using
different extractants. Extraction conditions were the same as in Fig. 1
maximum extraction yield from wet microbes was obtained
with methanol, followed by absolute ethyl alcohol, isopropanol, acetic acid, and acetonitrile. Obviously, the extraction amounts obtained from dichloromethane, n-hexane, and
petroleum ether were significantly lower than those obtained
from the other organic solvents (P < 0.05). However, each of
the extraction yields from wet cells was less than that of the
control. This may be because the presence of water reduced
the extraction rate.
Effect of water content on extraction yield
Extraction from wet cells was conducted using methanol
and ethanol solutions containing different water content,
respectively. Figure 3 shows that the extraction amounts of
menaquinones extracted gradually increased with a reduction in water content in both methanol and ethanol systems.
The extraction yields obtained using methanol were significantly less than those for ethanol when the content of
organic solvents was less than 95%, while they were slightly
higher than those of ethanol when the content was exceeded
95% (P < 0.05). However, each of the menaquinone yields
obtained from wet cells was less than that of the positive
control.
Fig. 3 Effect of different water contents on extraction yields of
menaquinones using methanol and ethanol
ratio of 6:1 (v/m) each time. Compared to that of the positive control, the highest recovery efficiency of menaquinones
reached 102.8%, which was much higher than that of the
negative control (93.3%) (P < 0.05).
As shown previously, the water content had a significant effect on the extraction yield from wet cells. Moreover, the amount of time required to extract the maximum
amount of menaquinones from wet cells is an important
parameter to consider. Wet cells samples were pretreated
with absolute ethyl alcohol for 10, 20, 30, and 40 min,
and extracted twice with methanol for 30 min (Fig. 5).
The results showed that pretreatment with absolute ethyl
alcohol from 10 to 40 min gave a significant improvement
with the highest extraction efficiency occurring at 30 min
(P < 0.05). The extraction rates were almost equal from 30
Effect of improved extraction procedures for wet cells
To improve the extraction yields of menaquinones directly
from wet biomass, we pretreated the wet microbes using
absolute ethyl alcohol at different ratios (v/m). The results
indicated that the pretreatment could significantly enhance
the extraction yields of menaquinones (Fig. 4). The highest
yield was obtained by extracting twice using methanol at a
13
Fig. 4 Effect of pretreatment of wet cells with different volume-tomass ratios on the recovery of menaquinones (pretreatment once with
ethanol and extraction twice with methanol)
Bioprocess Biosyst Eng
Discussion
Effect of extraction of menaquinones from dry and wet
microbes
Fig. 5 Effect of different pretreatment times using ethanol on the
recovery of menaquinones
to 40 min and stabilized after 30 min. Therefore, a 30-min
pretreatment time was an optimal preprocessing time.
Separation of the menaquinone homologs
The polarity of the organic solvent was an important
consideration for the separation of the menaquinone
homologs. Several factors including the flow rate of the
eluent, the ratio of height to diameter, and the recovery
rate of menaquinones played important roles in the separation. In the present study, the menaquinone homologs,
that is, MK-4, MK-5, and MK-6, were effectively separated using methanol, absolute ethyl alcohol, or acetonitrile in a glass reverse-phase C18 silica gel column
(Table 1). The results showed that the flow rate and recovery ratio using methanol were higher than those for both
absolute ethyl alcohol and acetonitrile, but the content of
menaquinones per mass of silica gel was lowest. Taking
the high value of the menaquinones and the reusability
of the silica gel into account, methanol was selected as
the optimum eluent.
Mass spectra yielded m/z values of 467, 535, and 603
for MK-4, MK-5, and MK-6, respectively, indicating that
all of them were detected as Na+-associated ion species
and corresponded to the menaquinone homologs (Fig. 6).
Table 1 Optimization of
separation of menaquinone
homologs using different
organic solvent in a glass
reverse-phase C18 silica column
In this study, we identified a single organic solvent for
extracting menaquinones from dry cells. The highest extraction yield was obtained using methanol among the selected
organic solvents, most likely due to the fact that methanol
has the highest polarity index among the solvents tested
in accordance with a previous study [15]. However, the
pretreatment process required drying equipment and was
time-consuming.
The results of extraction from wet cells showed that the
extraction yields obtained using methanol, absolute ethyl
alcohol, and isopropanol were significantly higher than those
obtained using dichloromethane, n-hexane, and petroleum
ether, indicating that the polarity of the organic solvent has
a substantial effect on the extraction efficiency. On the other
hand, the extraction yields of the organic solvents containing an –OH group, such as methanol, ethanol, and isopropanol, were higher than those of other solvents except for
n-butanol. This was probably because the –OH group could
form a covalent bond with the water contained in the wet
cells, thereby facilitating the infiltration of organic solvents.
Moreover, the yields of menaquinones extracted from the
wet cells directly using organic solvents were lower than
that of the control. It is probable that the water contained in
the samples reduced the capacities of the organic solvents
to break down or dissolve the cell walls, thus leading to low
extraction yields of menaquinones. Obviously, this method
was able to extract menaquinones from wet microbes, but
with lower yields than that of the control for 3 h at least.
In addition, tedious purification and separation steps were
required to obtain high recoveries of menaquinones from the
fermentation media. Therefore, it is necessary to develop
a rapid and efficient extraction method for menaquinones.
Effect of water content on extraction
A previous study showed that several variables, including
the percentage of solids in the cell slurry, the polarity of the
organic solvent, and the ratio of solvent to cell slurry volume, have a substantial effect on extraction efficiency [18].
Organic solvent
Content of menaquinones/
mass of silica gel (μg/g)
Flow rate
(mL/min)
Height–diameter
ratio (cm: cm)
Recovery ratio
of menaquinones
(%)
Methanol
Absolute ethyl alcohol
Acetonitrile
54.5
203.6
131.5
0.52
0.16
0.69
5.5: 1
14.0: 1
5.4: 1
99.6
98.7
98.9
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Bioprocess Biosyst Eng
Our results showed that the extraction yield obtained using
absolute ethyl alcohol was higher than that obtained using
methanol when the water content was more than 5%, indicating that absolute ethyl alcohol had a better dewatering effect
on the wet cells. However, the extraction yields obtained
using both methanol and ethanol appeared to be equal when
the water content was less than 5%, indicating that methanol
afforded a better permeability of the cell wall or membrane.
Therefore, absolute ethyl alcohol was applied as a dehydrating agent, and methanol was used as the extractant in the
following experiments.
Effect of improved extraction procedures for wet cells
The objective of this study was to develop an efficient solvent extraction method for recovering menaquinones from
wet cells of Flavobacterium. To reduce the energy input, all
extraction operations were carried out at room temperature
without agitation. Two variables, the ratio of solvent to cell
slurry mass and extraction time, were optimized. Compared
to a conventional solid-phase extraction technique [7, 8], a
liquid–liquid extraction technique [2, 6, 9, 10], or a supercritical fluid extraction technique [11–13], our method offers
three distinct advantages (1) a rapid and simple pretreatment
procedure; (2) a single and simplified organic solvent that is
conveniently recovered and cyclically used; (3) no requirement of considerable energy input or expensive devices.
Apparently, simplicity, speed, efficiency, environmental
friendliness, and inexpensiveness make our method suitable not only for laboratory-scale but also for industry-scale
processes.
Separation of the menaquinone homologs
Fig. 6 Mass spectra of menaquinones isolated from Flavobacterium.
a MK-4; b MK-5; c MK-6. The conditions of mass spectrometry were
as follows: ESI capillary voltage at 3.5 kV; mass spectrometry temperature: 350 °C; MK-4, MK-5, and MK-6 concentrations: 100, 100,
and 300 mg/L; injection volume: 2 μL
13
Several methods have been reported for separating menaquinone homologs, including thin-layer chromatography methods [7, 19] and high-performance liquid chromatography
(HPLC) methods [15, 17, 20–22]. However, theses separation methods are associated with several problems. The
quantity of menaquinone sample obtained by thin-layer chromatography is too little to meet the needs of downstream
experiments. Similarly, a menaquinone sample obtained
with HPLC is dissolved in several organic solvents and this
increases the difficulty of recovering each kind of organic
solvent recovery. Moreover, these separation methods for
menaquinones are merely suitable for experimental analysis
in the laboratory rather than for an industrial production process in a factory. Obviously, our method has overcome such
drawbacks and can be conveniently applied to separating
menaquinone homologs. This separation method could also
be used as one of the steps in the purification of menaquinone homologs.
Bioprocess Biosyst Eng
Conclusion
The extraction method from wet cells demonstrated here
represents a process that can greatly decrease the energy
input and the time required for sample pretreatment. Of
the solvents screened, methanol had the highest extraction
efficiency, approaching 102.8%, at a ratio of 6:1 (v/m) for
30 min each time, with pretreatment using absolute ethanol
at a ratio of 6:1 (v/m) for 30 min. The separation of menaquinone homologs, MK-4, MK-5, and MK-6, was carried out
by using a single organic solution. Obviously, this method is
advantageous for the recycling of reagents on a large scale.
Acknowledgements This work was financially supported by the Key
863 Fund of China (2014AA021704) and Natural Science Foundation
of Anhui Province (1308085MA07, 1608085QC46).
Compliance with ethical standards
Conflict of interest
interest.
All authors declare that they have no competing
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