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Transcript
Improved production of poly-γ-glutamate by newly Bacillus subtilis 115 with
high genetic competence
Fengqing Wang*, Jinzhong Liang,Dawei Fu,Wei Wang
Key Laboratory of Food Science and Engineering,College of Food Engineering,
Harbin University of Commerce, Harbin city, Heilongjiang 150076, People,s Republic
of China.
*E-mail address: [email protected].
Abstract:A bacterium with high poly-γ-glutamate (γ-PGA)productivity was isolated
from the traditional Japanese natto. This bacterium was classified as a Bacillus
subtilis and designated B. Subtilis115. It harbors no plasmid with both naturally high
γ-PGA productivity and genetic competence.Glutamate racemase gene(pgsE) was
cloned and glutamate racemase activity was confirmed to have the possibility of
existence in the cells,suggesting that the enzyme is involved in the D-glutamate
supply.L-Glutamate significantly induced γ-PGA production, and highly molecular
weight γ-PGA were synthesized. The volumetric yield reached 32.06 g/L in the
presence of 7% monosodium glutamate. Molecular sizes of γ-PGA were changed by
the salt concentration in the medium; γ-PGA with comparatively low molecular
masses were produced in culture media containing high concentrations of NaCl.
Culture parameters for highly productivity of γ-PGA were optimized. The yield of
γ-PGA and viscosity of broth could reach to 33.8 g/L and 640mpa.s, respectively,with
no pH control,3.0 L/min aeration and 150 rpm agitation for 72h.Due to the existence
of the degrading enzyme(GGT and PgdS), the fermentation period was strictly
controlled on the basis of the residual glucose concentration in the fermentation
broth.An amplicon of 2807bp represents the γ-PGA-coding genes(pgsBCA) was
obtained and sequenced.pgsB gene was cloned and expressed in Escherichia coli as
the key gene of γ-PGA synthesis.
Key words:poly(γ-glutamic acid);Bacillus subtilis;Culture condition;pgsBCA genes;
1.Introduction
Polyglutamic acid (PGA) is a biodegradable, non-immunogenic and unusual
anionic homopolyamide that is made of D- and L-glutamic acid units(Shih,
2001).γ-PGA depending on the attachment of the α-amino and γ-carboxy group.
γ-PGA can either be composed of only L-glutamic acid residues (γ-L-PGA), only
D-glutamic acid residues (γ-D-PGA) or both L- and D-glutamic acid residues
(γ-LD-PGA). The molecular weight of γ-PGA varies from 100kDa to
2000kDa.γ-PGA is different from proteins, because glutamate is polymerized inside
the cell via the γ-amide linkages and thus is synthesized in a ribosome-independent
manner (Akagi, T.,2007;Bajaj, I. B.,2008). Hence, substances that inhibit translation
of proteins, such as chloramphenicol, have no effect on the production of γ-PGA. Due
to the γ-linkage of its component glutamate residues, γ-PGA is resistant to proteases,
which cleave a-amino linkages(Candela,T.,2006).
γ-PGA was first discovered by Ivonovics and Bruckner(Ivanovics, G.,1937ab)
when a capsule of Bacillus anthracis was released into the medium upon autoclaving
1
(Shih, 2001).Another naturally occurring source of γ-PGA is the mucilage of natto
(fermented soybeans – a traditional food in Japan),which contains a mixture of γ-PGA
and fructan produced by Bacillus subtilis Sawamura(Shih, 2001;Candela, T.,2009) .
γ-PGA is produced mostly by Grampositive bacteria, which include the genus
Bacillus. It has also been reported that at least one Gram-negative bacterium
(Fusobacterium nucleatum), some archaea and eukaryotes have the ability to produce
γ-PGA(Candela, T.,2009;Weber, J.,1990;Hezayen, F. F.,2001) . γ-PGA has also been
found in neurons of mice where it was covalently linked to tubulin(Eddé, B.,1990).
Efforts have been made to insert the genes responsible for γ-PGA production into
Escherichia coli and plants such as tobacco to gain more knowledge regarding the
molecular mechanism of γ-PGA production(Tarui, Y.,2005;Ashiuchi, M.,1999) , and
pgsB, pgsC and pgsA genes were identified as essential for its roduction. Recently,
Cao et al.(Cao, M.,2013)also cloned and coexpressed the pgsBCA genes and
glutamate racemase gene (racE/glr) into E. coli, and reported that the engineered
E.coli strains had the ability to synthesize γ-PGA with excellent D-glutamate content
due to racE integration.
γ-PGA is an extremely important substance that has been exploited for a wide
array of useful applications due to its unique properties,such as food, cosmetics,
medicine, agriculture,oil recovery,water treatment and so on(Yasuzawa,
M.,2011;Osera, C., 2009;Wang, Q.,2008;Kurosaki, T.,2009;Inbaraj, B. S.,
2011;Ben-Zur, N.,2007;Inbaraj, B. S.,2012;Bhat, A. R., 2013;Lim, S., 2012;Tsao, C.
T., 2011;Shyu, Y., 2010).The number of potential application for γ-PGA is still
increasing.
In this paper, the aims of this research were to isolate and identify new microbial
sources of γ-PGA, characterize them, and optimize culture conditions for highly
productivity of γ-PGA. The genes encoding γ-PGA was amplified,sequenced and
cloned in Escherichia coli with the objectives of overproducing the polymer to suit
commercial applications.
2 Materials and methods
2.1 Preparation of corn saccharification liquid
The saccharification of corn starch was catalyzed by the double enzymes
method. Corn powder,mixed with water in the tank by 1:3,were liquefied at 85℃ for
30min at pH 6.7-7.0 using the commercial thermostable α-amylase with an enzyme
activity of 20KU/g.The temperature was rapidly decreased to about 60℃ ,and then the
pH of corn saccharification liquid was adjusted to 4.5 with hydrochloric acid.
Monosaccharide was formed using the commercial glucoamylase with an enzyme
activity of 50KU/g for 4h. The reducing sugars, cellulose, and protein (weight ratio
about 70:11:4) are the main components in the corn hydrolysate. The glucose
monomer fraction after pre-saccharification was close to 25%. The level of release of
glucose and nutrients (including protein) depended on saccharification time. Complete
starch hydrolysis required more than 7 h of pre-saccharification time.
2.2 Isolation and screening of γ-PGA-producing strains
The bacterial in the soil, Chinese traditional fermented soybean, fermented bean
curd, Japanese natto and other fermented bean products were enriched cultivated in
2
medium MS,which was composed of 1.5% yeast extract,2.8% beef extract,6.5%
glucose,3% soy peptone,0.3% KH2PO4,0.3% anhydrous sodium acetate,0.2%
ammonium
citrate,0.15%(v/v)
Tween80,1%
MgSO4•7H2O,0.5g/L
MnSO4•4H2O,1.92%
whey
powder,0.95%
casein
hydrolyzate,
1.91%
polyfructose.The culture solution were streaked onto Luria-Bertani (LB) agar plates
containing 2% L-glutamic acid ,1.5% (w/v) agar and cultured at 37°C for 72 h.The
bacterium was isolated from a highly mucous colony. Those bacterium were
inoculated into 5 ml of LB medium and cultivated at 37°C for 20 h in a rotatory shaker
at 150 rpm.In order to obtain a strain which could used corn saccharification liquid
as the carbon source instead of glucose,the seed liquid was transferred to 250 mL
Erlenmeyer flasks with 25mL fermentation medium composed of 5% L-glutamic
acid,25mL(v/v)corn saccharification liquid (sugar degree 200.00g/L),0.4%
peptone,1%NaCl.After culturing in a rotary shaker at 150 rpm and 37℃ for 48h,the
concentration of γ-PGA in fermentation broth was measured and the bacterium with
high yield was chosen for γ-PGA production.All shake experiments were run in
triplicates.
The strain was kept as lyophilized reference stocks in the China General
Microbiological Culture Collection Center(CGMCC2283).For working purposes,
bacterial were kept in 20% glycerol at -20°C. The strain was reactivated twice in LB
broth, streaked onto LB agar plates and subcultured onto LB slants. Strain slants were
kept under refrigeration until usage.
2.3 Identification and characterization of γ-PGA producer strain
The best producer of γ-PGA was characterized and identified by 16S rDNA
analysis and by morphological and physiological characteristics. DNA from a bacterial
was extracted using the TIANamp Bacteria DNA Kit(TIANGEN) following the
manufacturer instructions. PCR reaction was performed using the primers(10 μmol/L)
1 μL,10×PCR Buffer 5 μL,dNTP mixture 3 μL,Taq@ HiFi DNA polymerase(5
U/μL)1 μL and added ddH2O to 50 μL. The 16S rDNA was amplified using
primers(27Fp6:AGAGTTTGATCCTGGCTCAG;1492R:GGYTACCTTGTTACGAC
TT),PCR products were separated by agarose gel electrophoresis and the ethidium
bromide-stained bands were visualized under UV light and taken pictures with gel
imaging system(SIM International Group Co., Ltd). After confirmation, the remaining
PCR mix was purified using TIANgel Midi Purification Kit (TIANGEN) and
submitted to Sangon Biotech(Shanghai)Co.,Ltd for sequenced. Following sequence,
the nucleotide sequence was subjected to BLAST sequence analysis using the NCBI
(National Center for Biotechnology Information) website, and the nucleotide sequence
was deposited in GenBank database.Morphological and biochemical characterization
was performed according to the Manual of Bergey (Sneath PHA,1986) , and also
included additional references.
2.4 Analytical procedures
The concentration of extracellular γ-PGA was determined by alcohol
precipitation(LIANG Jin-zhong,2013).The concentration of L-glutamic acid and
glucose was measured by SBA-40D Bio-sensor with glucose oxidase electrode and
L-glutamic acid oxidase(Shandong Science Academic Biological Institute, PR
3
China).The value of pH was read from the monitor of fermentor.The viscosity of the
culture broth was measured by Digital Viscometer with a spindle SP-2 at
25℃(DNJ-5S,China).
2.5 The genes cloning and expression
B. Subtilis115 and Escherichia coli were cultured at 37℃ in LB medium,which
containing 0.5% (w/v) yeast power,1.0% (w/v) peptone,1.0% (w/v) sodium chloride.
Ampicillin (100 mg/mL) was added to the medium when required. Escherichia coli
trans1 was used for plasmid construction and Escherichia coli BL21(DE3) was
transformed for pgsB expression.The plasmid of pET22b(+) is the shuttle
vector,containing ampicillin resistance gene.The primers as follows:
pgsBCA-F:CGGGATCCATGTGGTTACTCATTATAGCC;pgsBCA-R:CCCAAGC
TTTTATTTAGATTTTAGTTTGTCAC;pgsB-F:CGGGATCCTGTGGTTACTCATTA
TAGCCTGTGCTG;pgsB-R:CCCAAGCTTGCTTACGAGCTGCTTAACCTTG;pgsEF:CGGGATCCATGAAATTTGTCAAAGCTATCTGGC;pgsE-R:CCCAAGCTTTTTAT
TGGCATTTACCGGTTC;ggt-F:CGGAATTCATGAAAAGAACGTGGAACGTCTG;ggtR:CGGCGGCCGCTTTACGTTTTAAATTAATGCCGATC;pgdS-F:CGGAATTCGTGAA
CACACTGGCAAACTG;pgdS-R:CGGCGGCCGCTTGCACCCGTATACTTCCTGC;
3 Results and discussion
3.1 Screening and identification of γ-PGA-producing strains
Of γ-PGA producer selected isolates, the number 115 strain which showed the
highly mucous colony on isolation medium and produced high quantity of γ-PGA
polymer in liquid medium (data not shown)was selected and intensely studied.The
nucleotide sequence of 16S rDNA was compared to available sequences at NCBI
GenBank database, and revealed 99% of similarity with several B.subtilis and
Bacterium, and also to some Bacillus tequilensis and Bacillus amyloliquefaciens.
Taxonomic studies have indicated that Bacillus species are very similar to each other
with respect to 16S rDNA, and B. amyloliquefaciens is indeed closely related to
B.subtilis on the basis of 16S-23S ITS nucleotide sequences(Porwal S,2009;Xu
D,2003;Sumpavapol P,2010).Nevertheless,some physiological characteristics allowed
distinguishing among these species(Sneath PHA,1986;Sumpavapol P,2010;Priest
FG,1988; Reva ON,2001;Welker NE,1967;Kim KM,2009). The morphological and
physiological characterization of 115 strain showed that it is aerobic, rod-shaped,
spore-forming, catalase-positive, Gram(+) bacterium, capable of producing acid from
glucose, as a typical Bacillus sp.(Sneath PHA,1986). The positive citrate reaction and
oxidase test, growth at 50°C, no acid formation from lactose and sorbitol, and growth in
NaCl 7% but not in NaCl 10 % allowed for different from other Bacillus species and for
the identification of 115 as B. subtilis. All morphological and physiological
characteristics for B. subtilis115 strain are shown in Table 1.
Table 1 Physiological and morphological characterization of Bacillus subtilis 115
Characteristics
Results
Characteristics
Shape
Rod
Acid from
Gram stain
+
Glucose
+
Sporulation
+
L- arabinose
+
Nitrate reduction
+
Lactose
-
4
Results
Hydrolysis of
Raffinose
-
Starch
+
Mannitol
+
Casein
+
Sorbitol
-
Gelatin
+
Growth at pH5.7
+
Indole formation
-b
Growth at 50 °C
+
Voges-Proskauer test
-
Growth in 7 % NaCl
+
Citrate utilization
+
Growth in10 % NaCl
-
Catalase test
+
Oxidase test
+
Phenylalanine desaminase
-
+:Positive ;- Negative
3.2 Natural genetic competence of B. subtilis 115
Most B.subtilis (natto) harbor plasmid(s)(Meijer et al.1998) and are particularly
unsuitable strains for genetic manipulation because of their lack of, or only
slight,competence(Ashikaga et al. 2000). Thus, we examined whether B.subtilis115
harbors plasmids.DNA of B.subtilis115 was extracted by the method for plasmid
preparation (Ashiuchi et al.1999);agarose gel electrophoresis revealed no band
corresponding to a plasmid.PCR amplification of the rep gene, which is highly
conserved in the B.subtilis (natto)plasmids(Meijer et al. 1998), was also negative. We
thus judged B. subtilis 115 to be a plasmid-free γ-PGA producer. Thus,as long as we
searched for a useful genetic marker,it is possible to constructed a transformable
B.subtilis (natto) strain by genetic modification.
3.3 Glutamate-inducible γ-PGA production by B. Subtilis115
γ-PGA-producing bacteria are divided into two groups:glutamate-dependent and
glutamate-independent producers(Kunioka 1994; Ito et al. 1996). In the former, the
γ-PGA yield indeed increases upon addition of glutamate to the medium, but the
bacteria can produce considerable γ-PGA even in the absence of glutamate because of
the operation of the de novo pathway of L-glutamate synthesis (Kunioka 1994). We
examined the effect of glutamate on γ-PGA production by B. subtilis 115. As shown
in Table 2,Bacillus subtilis 115 depended on extracellular glutamate,it would not
produce γ-PGA without glutamate in medium.The amount of γ-PGA increased with
increasing glutamic acid addition to the medium,while the cell growth and cultrue
broth viscosity decreased.It was a linear relationship between the molecular weight of
γ-PGA and viscosity of the fermentation broth(data was not shown).In order to
achieve high molecular weight γ-PGA,the concentration of sodium glutamate was
chosen to add 7% in the production process.After a 48h incubation in the presence of
7% sodium glutamate, the γ-PGA yield reached 32.06 g/L.
Table 2
Effect of monosodium glutamate concentration on γ-PGA formation in Erlenmeyer flasks.
CDW
γ-PGA
Residual glucose
Residual glutamate
Cultrue broth viscosity
(g/L)
(g/L)
(g/L)
(g/L)
(mPa·s)
0
1.99
0
48
0
0
10
3.12
8.63
0
3
135
20
3.26
11.74
0
11
210
monosodium
glutamate
(g/L)
5
30
3.18
14.52
0
20
360
40
3.64
16.77
0
30
510
50
3.90
22.46
1
37
600
60
4.01
24.77
2
45
861
70
4.17
32.06
6
54
870
80
3.50
31.18
11
64
660
90
3.22
30.11
15
71
525
100
3.92
29.82
15
78
240
The D-glutamate content was over 50% in every γ-PGA produced under the
conditions used, suggesting that the bacterium possesses a synthetic pathway to
produce D-glutamate, the main precursor of γ-PGA, from L-glutamate.To obtain a
clue as to the nature of the D-glutamate synthetic pathway in B. subtilis 115, we
attempted to clone the gene of glutamate racemase(pgsE) from the cells.As a result,
the pgsE was successfully cloned(Fig.2).
3.4 Effects of salt on γ-PGA production
We investigated the effects of salt on γ-PGA productivity of B.subtilis115 using a
medium containing 7% monosodium glutamate and various concentrations of NaCl
and found that the apparent viscosity of the culture medium increased and then
decreased with increasing in salt concentration as showed in Fig.3. We also found the
molecular weight of γ-PGA was positively correlated with the viscosity of
fermentation broth(data not shown).The γ-PGA yields under the conditions tested:
30.4, 26.6, 32, 32.8 and 33.6g of γ-PGA were obtained per 1L of culture media
containing 0.05, 0.5, 1, 1.5 and 2% NaCl, respectively.γ-PGAs with quite high
viscosity(high molecular sizes)were synthesized in media containing concentrations
of NaCl (1.5%).In contrast, under high saline conditions (2%),γ-PGA of
comparatively low viscosity(low molecular sizes)were preferentially produced.
3.6 Effects of culture condition on γ-PGA production
The importance of initial pH control to achieve efficient conversions of carbon
sources to polymer products has been well documented for another microbial
fermentation process(Moraine RA,1971).In order to evaluate the effect of initial pH
and the necessity of pH control in the fermentation process on the γ-PGA production,
fermentations were carried out under different initial pH and no pH control at 37°C
for 48h.The pH of the culture medium was adjusted to 4.0-7.5 using 6 mol/L HCI and
10 mol/L NaOH. As shown in Fig.4, the yield of γ-PGA synthesis were observed at
initial pH 4.0, 4.5, 5.0, 5.5, 6.0,6.5,7.0. The pH of the broth under no pH control was
gradually decreased from 5.91 to 5.5 before 24 h and then gradually increased to 5.9
till the end of fermentation. Cromwick and co-workers(Cromwick AM,1996) reported
that in the cultivation of B. licheniformis ATCC 9945,the pH was acidified from 7.4
to 5.6 between 48 and 96 h,at 37 °C,but B. subtilis 115 produced the highest
concentration of γ-PGA under no pH control fermentation. As reported for B.
licheniformis CCRC 12826(Shih IL,2001), where the initial pH of 6.5 dropped to 5.6
after 36 h of cultivation at 37 °C. Although pH played an important role in the γ-PGA
production by other Bacillus strains, the experiments in this study indicated that strict
6
control of pH was not necessary.On the contrary, the rule of pH changing could be
used to determine the fermentation was normal or not.In addition, the highest
viscosity of the culture broth was also observed at no pH control fermentation.
Therefore,further experiments were carried out without pH control during
fermentation.
The dissolved oxygen has been recognized as an important factor in aerobic
fermentation affecting the nature and/or rate of metabolic product formation.
Dissolved oxygen is often controlled by ventilation, stirring speed and tank pressure
and fermented liquid properties of many factors in the fermentation process. Since
γ-PGA is an extracellular polymer, the culture broth becomes highly viscous with
γ-PGA production. The increased viscosity usually inhibits volumetric oxygen mass
transfer, which leads to oxygen limitation. A similar phenomenon has been reported
for xanthan, where it was shown that its volumetric yield could be improved by
increasing the available oxygen through increased agitation rate and oxygen partial
pressure in the air pumped through the fermentation vessel[43]. The fermentations
were carried out at several aeration rates (0-3.0 L/min) and different agitation to
evaluate the effect of oxygen on the γ-PGA production. As shown in Fig.5(AB),
enhanced the rate of glucose consumption and γ-PGA synthesise were observed when
aeration rates increased.The cell growth rate was fast, and the fermentation period was
shortened.As shown in Fig.6, although the maximum rate of glucose consumption was
observed at 300 rpm, γ-PGA concentration and viscosity were low at this agitation
speed. This result might be due to high shear stress from the relatively rapid agitation
rate. Further experiments were carried out at aeration rate of 3.0L/min and agitation
speed of 150 rpm.
As shown in Fig.7, the viscosity of fermentation broth was gradually increased
until the glucose was completely consumption,and then decreased with the extension
of fermentation time.Jeong JH reported(Jeong JH,2010)the molecular weight of the
γ-PGA produced was decreased at the end of fermentation.The reduction of γ-PGA
molecular weight at the end of fermentation might be due to γ-PGA depolymerase
activity, which was verified by cloned the γ-PGA degrading enzymes gene(pgdS and
ggt) in this study.The degradation of γ-PGA is considered to be the result of the
synergistic action of PgdS and GGT enzyme(Kimura and Fujimoto, 2010; Kimura et
al., 2004; Yao et al.,2009).The physical and chemical properties of PgdS and GGT
were predicted online based on its amino acid sequence,as shown in Table
3,respectively.Ashiuchi M(Ashiuchi M,2003)and Suzuki andTahara(Suzuki
T,2003)previously reported that the molecular weight of γ-PGA depolymerase from B.
subtilis was 42 kDa and 44 kDa, respectively. γ-PGA depolymerase from B. subtilis
RKY3 was relatively more expressed at the end of fermentation than the beginning of
fermentation(Gwi-Taek Jeong,2014).Troy(Troy FA,1973)found B. licheniformis
expressed γ-PGA depolymerase at the late stationary phase. Kunioka and
Goto(Kunioka M,1994) also reported that B. subtilis IFO 3335 expressed γ-PGA
depolymerase when cultivated in a medium containing only γ-PGA as the
substrate.The concentration of glucose which is necessary for microbial growth
energy and carbon sources,close to zero at the late of fermentation. γ-PGA as the only
7
substrate,the promoter of γ-PGA depolymerase gene was activated and induced
expression at this time.
Table 3 Analysis of physicochemical properties on γ-PGA degrading enzymes proteins
Physicochemical properties
PgdS
GGT
Formula
C2056H3172N526O611S6
C2869H4520N752O881S17
Molecular weight
45227.3
64188.9
Number of amino acids
413
587
Theoretical pI
8.78
5.57
Total number of negatively charged
36
75
41
65
23.00
33.19
-0.215
-0.348
residues (Asp + Glu)
Total number of positively charged
residues (Arg + Lys)
Instability index
Grand
average
of
hydropathicity
(GRAVY)
3.5 Amplification of B. subtilis 115 specific γ-PGA biosynthesis genes (pgsBCA)
using specific primer PCR
The pgsBCA gene was amplified by PCR from B. subtilis115 as templet.As
shown in Fig.9B,an amplicon of 2807bp was obtained.PCR fragment was purified and
ligated in cloning vector pET22b(+).The sequence of pgsBCA genes was determined
and shown in Fig.9A,the DNA sequence comprises three open reading frames (ORF),
pgsB 1182 bp, pgsC 450 bp and pgsA 1143 bp(Fig.9).
Current research supports the idea that γ-PGA synthetase is a membrane-associated
modular protein complex (viz., PgsBCAE) with a Rossmann-type amide ligase-like
PgsB component (Ashiuchi, M.,1999;Ashiuchi et al.,1999; 2001b; Urushibata et al.,
2002). γ-PGA was synthesized at the active site of the synthase complex (PgsBCA).
PgsB and PgsC together form most parts of the complex’s catalytic site, whereas
PgsA seems to remove the elongated chain from the active site so that the next
monomer can be added and may also be involved in transporting γ-PGA (Ashiuchi et
al., 2001;Urushibata et al., 2002).Therefore, the expression of pgsB in E. coli was
research as the key gene of γ-PGA synthesis.The pgsB gene was cloned on expression
vector pET22b(+) and then expressed in E.coli BL21(DE3). Ampicillin was used to
induce expression for 4h and the cell was collected by centrifugation.The degree of
pgsB gene expression was investigated by polyacrylamide gel electrophoresis(Fig.10).
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