- Original article
- Open Access
Construction of efficient Streptococcus zooepidemicus strains for hyaluoronic acid production based on identification of key genes involved in sucrose metabolism
© The Author(s) 2016
- Received: 20 November 2016
- Accepted: 22 November 2016
- Published: 28 November 2016
Biosynthesis of polysaccharide hyaluoronic acid (HA) by Streptococcus zooepidemicus is a carbon-intensive process. The carbon flux and factor(s) restricting HA yield were not well understood. Here, we investigated the function of genes involved in sucrose metabolism and identified targets limiting HA yield, which were exploited to construct efficient S. zooepidemicus strains for HA production. The sucrose uptake was addressed by deletion of scrA and scrB, which encodes sucrose-PTS permease and sucrose-6-phosphate hydrolase, respectively. We found that scrB was essential for the growth of S. zooepidemicus and HA biosynthesis, and accumulation of sucrose-6-phosphate was toxic. ΔscrB could not grow in THY-sucrose medium, while ΔscrA and ΔscrAΔscrB showed negligible growth defects. Overexpression of scrA significantly reduced biomass and HA production, while overexpression of scrB resulted in 26% increase of biomass and 30% increase of HA yield. We revealed that fructose-6-phosphate for HA biosynthesis mainly originates from glucose-6-phosphate. Deletion of scrK, a gene encoding hexokinase, led to 11% reduction of biomass and 12% decrease of HA yield, while deletion of hasE, a gene encoding phosphoglucoisomerase, resulted in the abolishment of HA biosynthesis and a significantly slow growth. We found that HA biosynthesis could be improved by directing carbon flux to fructose-6-phosphate. Deletion of fruA encoding the EII of fructose-PTS and fruK encoding phosphofructokinase showed no apparent effect on cell growth, but resulted in 22 and 27% increase of HA yield, respectively. Finally, a strain with 55% increase of HA was constructed by overexpression of scrB in ΔfruK. These results provide a solid foundation for further metabolic engineering of S. zooepidemicus for highly efficient HA production.
- Hyaluoronic acid
- Metabolic engineering
- Streptococcus zooepidemicus
Hyaluronic acid (HA) is a linear polysaccharide consisting of 2000–25,000 repeating disaccharide units of d-glucuronic acid (GlcUA) and N-acetylglucosamine (GlcNAc) linking alternatively by β-1, 3 and β-1,4 glycosidic bonds (Chong et al. 2005). The high molar mass and unique viscoelastic and rheological properties render this natural biopolymer a broad range of biomedical and industrial applications (Kogan et al. 2007). HA is found in connective tissues of animals as well as in the capsules of various bacteria such as Streptococci and Pasteurella (Wessels et al. 1991). Conventionally HA was extracted from animal tissues like rooster combs, and now is increasingly produced by fermentation of Streptococcus zooepidemicus owing to the simple purification process and low production cost (Liu et al. 2008a, b; Chen et al. 2009a, b).
Microbial synthesis of HA is a carbon- and energy-intensive process (Chong and Nielsen 2003; Chong et al. 2005; Ruffing and Chen 2006). The synthesis of HA accounts for about 5% carbon source, while cell growth and production of lactic acid and acetic acid consume around 10% and 80% carbon source, respectively (Liu et al. 2008a, b). Precursors, such as uridine diphosphate-glucuronic acid and uridine diphosphate-N-acetyl glucosamine, for HA synthesis are also precursors for cell wall biosynthesis. Therefore, HA synthesis competes with the cell growth for carbon source and energy. It is reasonably expected that high yield of HA can be achieved by decreasing the competition of cell growth and inhibition effect of lactic acid on synthesis. Thus, optimization of nutrition and culture condition and use of various fermentation modes have been attempted to enhance HA yield in S. zooepidemicus (Liu et al. 2008a, b; Pires and Santana 2010).
The metabolic engineering approach has been explored to increase HA yield and control HA molecular weight in S. zooepidemicus. Overexpression of NADH oxidase resulted in 33% and 15% increase of ATP and biomass, respectively, but no improvement for HA yield was observed in S. zooepidemicus (Chong et al. 2005). Optimization of HA precursor levels using feeding or genetic engineering approaches can improve HA molecular weight (Chen et al. 2009a, b, 2014). Moreover, recombinant HA production has been exploited in various bacteria and yeast (Widner et al. 2005; Mao and Chen 2007; Yu and Stephanopoulos 2008; Liu et al. 2011; Jeong et al. 2014). Owing to the limited knowledge of gene function and physiology of S. zooepidemicus, few cases of desired increase of HA yield were reported using metabolic engineering strategy. Release of complete genome sequences of several S. zooepidemicus strains and successful development of a markerless gene-deletion system enable us to elucidate the role of individual genes in cell growth and metabolism, which will guide the metabolic engineering of S. zooepidemicus for HA production (Beres et al. 2008; Ma et al. 2011; Sun et al. 2013).
To identify target(s) for metabolic engineering of S. zooepidemicus, we extended the previous study of the HA biosynthesis pathway by systematically investigating the function of genes involved in sucrose uptake and metabolism. We found that scrB was essential for the growth and HA production in the presence of sucrose. Overexpression of scrB resulted in 15% increase of biomass and 23% increase of HA yield. fruA and fruK play important roles in the control of carbon flux to HA biosynthesis. Deletion of fruA or fruK resulted in 22% and 27% increase of HA yield respectively. Up to 55% increase of HA yield was achieved by overexpressing srcB in ΔfruK mutant cells.
Bacterial strains and growth conditions
All strains used in this study are listed in Additional file 1: Table S1. Streptococcus. equi subsp. zooepidemicus ATCC39920 (S. zooepidemicus) wild type (WT) and mutants were grown at 30 °C or 37 °C in Todd-Hewitt yeast (THY) medium (Sun et al. 2013) or chemically defined medium II (CDM2) (Armstrong and Johns 1997) Escherichia coli (E. coli) JM109 was grown at 37 °C in Luria–Bertani (LB) medium supplemented with antibiotics when necessary (Liu et al. 2007). The concentrations of antibiotics used in experiments were as follows: for E. coli, ampicillin (100 μg/mL), and spectinomycin (50 μg/mL), and for S. zooepidemicus, spectinomycin (100 μg/mL).
Gene deletion in S. zooepidemicus
Genes were deleted using a markerless gene-deletion system as described previously (Sun et al. 2013). Briefly, using S. zooepidemicus genomic DNA as the template, the upstream and downstream fragments of scrA were amplified by PCR and joined by splicing overextension (SOE) PCR. The PCR products were separated by 1% agarose gel electrophoresis, and subsequently excised from the gel and purified with Gel extraction Kit (Qiagen, Hilden, Germany). The resultant product was digested and ligated into the SalI/EcoRI sites of the vector pSET4s::sacB to obtain pSET4s::sacB::scrALR. S. zooepidemicus containing pSET4s::sacB::scrALR was first grown at 30 °C for 12 h and then further cultured at 37 °C for another 4 h in THY medium supplemented with 100 μg/mL spectinomycin. The culture was selected on THY medium supplemented with 5% (w/v) sucrose. The sucrose-resistant and spectinomycin-sensitive clones were isolated, and scrA gene-deletion mutants were examined by PCR and further confirmed by sequencing. The same strategy as used for scrA deletion was followed to construct other single-gene-deficient strains and double mutants. The primers used for construction of gene deletion cassettes and selection of mutants are listed in Additional file 1: Table S2. The restriction enzyme sites are underlined.
Generation of scrA or scrB overexpression strains
Genomic DNA of S. zooepidemicus was used as the template for cloning of scrA and scrB. In brief, the open reading frame (ORF) of scrA or scrB together with its 200 bp promoter region was amplified by PCR. After purification, the resultant products were digested and then ligated onto plasmid pLH243, a modified pSET4S vector, to obtain pLH243::scrA and pLH243::scrB, respectively. The fidelity of cloned sequence was confirmed by sequencing. pLH243::scrA or pLH243::scrB was introduced into wild-type S. zooepidemicus, ΔfruA or ΔfruK and then selected with spectinomycin to obtain transformants that express extra copy of scrA or scrB contained on the plasmid. The primers used for construction of scrA or scrB overexpression cassette are listed in Additional file 1: Table S2. The restriction enzyme sites are underlined.
Batch fermentation of S. zooepidemicus wild type and mutants was carried out in a 5-L bioreactor (Sartorius Stedim, Aubagne, France) with a working volume of 3 L as described (Chen et al. 2009a, b). The fermentation medium is composed of (per liter) 50 g sucrose, 3.5 g yeast extract, 10 g casein peptone, 2 g K2HPO4, 1.5 g NaCl, and 0.4 g MgSO4·7H2O. During fermentation process, the pH was maintained at 7.0 by automatic addition of 5 M NaOH, and temperature was controlled at 37 °C with agitation at a speed of 400 rpm and aeration volume 1.5 vvm. Flask experiments were conducted using 250-mL conical flasks (100 mL culture volume) containing sucrose -THY (in g/L: beef extract 10, casein tryptone 20, sucrose 2, yeast extract 2, NaHCO3 2, NaCl 2, Na2HPO4 0.4) with agitation (200 rpm) at 37 °C. The pH was initially set to 7.0 and adjusted every 2–3 h with sterile 5 M NaOH.
HA concentration was determined by the carbazole methods described previously (Bitter and Muir 1962), where the optical density (OD) was measured at 530 nm using a spectrophotometer (UV-2100 spectrophotometer). Cell concentration was determined by measuring the OD of the culture at 660 nm. The concentration of lactic acid was determined by Biosensing meter (SBA-40E). Sucrose concentration was determined by resorcinol method (Liu et al. 2008a, b). In brief, 0.9 mL sucrose sample mixed with 0.1 mL 2 M NaOH was incubated in boiled water for 10 min and then immediately cooled in running water. 1 mL 10 M resorcinol and 3 mL 10 M HCl were sequentially added into the mixture followed by incubation in 80 °C water for 8 min and then cooled to room temperature. The absorbance was measured at 500 nm and the sucrose concentration was determined by the standard curve.
scrB is essential for the growth of S. zooepidemicus on sucrose-containing media
We further performed growth assay on more complex media. All mutants grew as well as wild type on THY medium in which glucose was the main carbon source (Fig. 2c). Exclusion of glucose from THY medium did not make apparent differences to the growth of the mutants and wild type (Fig. 2d), suggesting that the minimal complex carbon source in THY medium is sufficient for the growth of these strains. Significantly, replacement of glucose with sucrose in THY medium resulted in growth inhibition of ΔscrA, ΔscrAΔscrB and abolishment of growth of ΔscrB (Fig. 2e). In liquid sucrose-THY medium, ΔscrA and ΔscrAΔscrB produced 45% less of biomass than wild type, and ΔscrB could not grow in this culture condition (data not shown). It is likely that ΔscrA and ΔscrAΔscrB use the complex carbon source for growth even in the presence of high concentration of sucrose since these mutants were unable of transporting sucrose into cell. In contrast, ΔscrB is able to transport sucrose into the cell and form sucrose-6-phosphate, however, it is incapable of hydrolyzing sucrose-6-phosphate. Based on above data, we speculate that scrB is essential for the growth of S. zooepidemicus in the presence of sucrose, and high concentration of sucrose-6-phosphate is likely toxic for S. zooepidemicus and inhibits cell growth.
Overexpression of scrB promotes S. zooepidemicus growth and HA biosynthesis
Fructose-6-phosphate is mainly from glucose-6-phosphate
Deletion of fruA or fruK increases HA yield
Overexpression of scrB in ΔfruA or ΔfruK strain enhances HA production
The role of the sucrose-specific PTS for sucrose metabolism has been studied in some detail (Reid and Abratt 2005). Our genetic characterization of srcA and scrB demonstrated that both of them are indispensible for the growth of S. zooepidemicus on CDM2 medium (Fig. 2b), in which sucrose is the sole carbon. ΔscrB grows well on complicated carbon source mixture glucose-THY medium, while it can not grow on sucrose-THY medium (Fig. 2c, e). The growth defect of ΔscrB can be complemented by plasmid-based expression of scrB complemented. It is likely that sucrose-6-phosphate accumulating intracellularly in ΔscrB as a consequence of uptake and phosphorylation of sucrose by ScrA is toxic for S. zooepidemicus. Similarly, growth of Corynebacterium glutamicum strains lacking sucrose-6-phosphate hydrolase was severely affected on a glucose–sucrose mixture (Engels et al. 2008). Streptococcus mutans mutant lacking sucrose-phosphate-hydrolyzing activity showed decreased growth in mannitol when sucrose was added to the culture medium (Zeng and Burne 2013). Thus, it could be a general phenomena that sucrose-6-phosphate is toxic for gram-positive bacteria.
Fructose 6-phosphate lies within the glycolysis metabolic pathway and is the substrate for the production of GlcNAc, the precursor of HA. Fructose 6-phosphate is produced by isomerisation of glucose-6-phosphate and phosphorylation of fructose by hexokinase or fructose kinase. S. zooepidemicus genome does not contain a gene encoding the putative hexokinase. Under sucrose environment, the deletion of hasE caused severe growth defects and the loss of HA production, while the deletion of scrK resulted in a marginal reduction in strain growth and HA production (Fig. 4a–c). The unexpected growth profile of ΔhasE and ΔscrK suggests that the function of hasE contributes most of the cellular fructose-6-phosphate level. S. zooepidemicus has two pathways for the metabolism of fructose, one is mediated by ScrK and the other is FruA and FruK. Deletion of fruA or fruK results in significant increase of HA production (Fig. 5c), suggesting that loss of either of these two genes likely promotes the carbon flux to HA biosynthesis. To further elucidate the underlying mechanism of fruA or fruK on HA biosynthesis, it will be necessary to investigate the expression profile of genes involved in HA biosynthetic pathway, the corresponding enzyme activity and the intermediate levels in fruA- and fruK-deficient strains.
Variant strategies, such increase of biomass and addition of intermediate chemicals, were explored to improve HA production in S. zooepidemicus (Chong et al. 2005; Liu et al. 2011). Alleviating the toxicity of metabolic intermediate promotes cell growth. Here, we found that overexpression of scrB significantly improves the growth and HA yield of S. zooepidemicus (Fig. 3b). Deletion of fruA or fruK likely increases fructose-6-phosphate level, resulting in increase of HA yield (Fig. 5c). Based on these finding, we constructed scrB/OP-ΔfruA and scrB/OP-ΔfruK strains, which showed significant increase in HA productivity (Fig. 6b). Compared with wild type, scrB/OP-ΔfruA and scrB/OP-ΔfruK produced less lactic acid, the side product, and had higher levels of residual sucrose (Fig. 6c, d). This suggests that both strains utilize sucrose more efficiently than wild type for HA biosynthesis. Recently, it is reported that down-regulation the expression of pfkA, a gene encoding phosphofructokinase, increase the HA yield in Bacillus subtilis (Jin et al. 2016). Here, we found that deletion of pfk in S. zooepidemicus results in inhibition of the growth and HA production (Fig. 5b, c). The distinct physiology of B. subtilis and S. zooepidemicus probably accounts for this difference.
In summary, our genetic investigation reveals that the function of scrB is essential for the growth of S. zooepidemicus and HA biosynthesis in the presence of sucrose. Characterization of ΔhasE,Δscrk,ΔfruA and ΔfruK revealed the role of these genes in carbon flux and HA biosynthesis. Guided by these finding, a high efficient scrB/OP-ΔfruK was constructed, which showed 26% increase of biomass and 55% increase of HA yield.
LH and ZX designed research; ZX, WM and FL performed research; LH, ZX, and CW analyzed data and wrote the paper. All authors read and approved the final manuscript.
We thank professor Lars Nielsen’s insightful suggestions. This work was supported by research foundation of Tianjin Science and Technology Commission (13RCGFSY19400), and the Tianjin Municipal High School Science and Technology Development Fund Program (20130602).
The authors declare that they have no competing interests.
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