Alternative production process strategies in E. coli improving protein quality and downstream yields

Process strategies for production of recombinant rhamnulose 1-phosphate aldolase (RhuA) in Escherichia coli were found to have an important impact on downstream processing when preparing the enzyme for its use as immobilized biocatalyst. First, a continuous inducer feed was implemented in substrate limited fed-batch cultures to overexpress RhuA with a hexa histidine-tag (6xHis-tag) at its N-terminus. The final specific RhuA level was 180 mg g⁻¹ DCW, but the final specific enzyme activity (1.7 AU mg⁻¹ RhuA) was considerably lower than expected. Only 55% of immobilization yield was achieved when immobilized metal affinity chromatography (IMAC) was used to purify and immobilize RhuA from cellular lysate in a single step. Western blot analyses showed that only 20% of overexpressed RhuA kept the whole 6xHis-tag at the end of the culture due to partial proteolysis. Two different growth strategies improved protein quality and immobilization yield:

(i) Temperature reduction to 28 °C in substrate limited operation decreased proteolysis and allowed higher specific activities, 210 mg g⁻¹ DCW. The enzyme activity increased to 4 AU mg⁻¹ RhuA and purification-immobilization yield to 93%.

(ii) A novel fed-batch operational procedure, working at high glucose concentration was implemented. High aldolase levels, 233 mg g⁻¹ DCW, were reached at the end of the culture. The final enzyme activity was also higher than 4 AU mg⁻¹ RhuA, and 95% of immobilization yield was achieved.

For both cases, Western blot analyses showed that 80–100% of overexpressed RhuA kept the whole 6xHis-tag at the end of the culture, confirming that recombinant protein quality had been improved.     

Simplified feeding strategies for the fed-batch cultivation of Kluyveromyces lactis GG799 for enhanced recombinant xylanase production

A xylanase gene (xyn2) from Trichoderma reesei ATCC 58350 was previously cloned and expressed in Kluyveromyces lactis GG799. The production of the recombinant xylanase was conducted in a developed medium with an optimised batch and with fed-batches that were processed with glucose. The glucose served as a carbon source for cell growth and as an inducer for xylanase production. In a 1-L batch system, a glucose concentration of 20 g L^?1 and 80 % dissolved oxygen were found to provide the best conditions for the tested ranges. A xylanase activity of 75.53 U mL^?1 was obtained. However, in the batch mode, glucose depletions reduced the synthesis of recombinant xylanase by K. lactis GG799. To maximise the production of xylanase, further optimisation was performed using exponential feeding. We investigated the effects of various nitrogen sources combined with the carbon to nitrogen (C/N) molar ratio on the production of xylanase. Of the various nitrogen sources, yeast extract was found to be the most useful for recombinant xylanase production. The highest xylanase production (110.13 U mL^?1) was measured at a C/N ratio of 50.08. These conditions led to a 45.8 % increase in xylanase activity compared with the batch cultures. Interestingly, the further addition of 500 g L^?1 glucose led to a 6.2-fold increase (465.07 U mL^?1) in recombinant xylanase activity. These findings, together with those of the exponential feeding strategy, indicate that the composition of the C/N molar ratio has a substantial impact on recombinant protein production in K. lactis.     

Characterization of a new multifunctional beta-glucosidase from <Emphasis Type="Italic">Musca domestica</Emphasis>

Objective

To engineer Pichia pastoris for heterologous production of cellulase from Musca domestica and explore its potential for industrial applications.

Results

A new beta-glucosidase gene (bg), encoding 562 amino acids, was cloned from M. domestica by using rapid amplification of cDNA ends. The gene bg was linked to pPICZαA and expressed in P. pastoris with a yield of 500 mg l^?1. The enzyme has the maximum activity with 27.6 U mg^?1 towards cellulose. The beta-glucosidase has stable activity from 20 to 70 °C and can tolerate one-mole glucose. It has the maximum activities for salicin (25.9 ± 1.8 U mg^?1), cellobiose (40.1 ± 2.3 U mg^?1) and cellulose (27.6 ± 3.5 U mg^?1). The wide-range substrate activities of the beta-glucosidase were further verified by matrix-assisted laser desorption/ionization mass spectra. Structural analysis shows that the beta-glucosidase belongs to glycoside hydrolase family Ι and possesses O-glycosylation sites.

Conclusions

Thus, a multifunctional beta-glucosidase was expressed from M. domestica and provides a potential tool for industrial application of cellulose.

     

Enhanced production of ATP-binding cassette protein exporter-dependent lipase by modifying the growth medium components of Pseudomonas fluorescens

The industrially-important thermostable lipase, TliA, was extracellularly produced in the recombinant Pseudomonas fluorescens by the homologous expression of TliA and its cognate ABC protein exporter, TliDEF. To increase the secretory production of TliA, we optimized the growth temperature and the culture medium of P. fluorescens. The total amount and the specific productivity of lipase was highest at 25 °C of cell growth temperature, although maximal cell growth was observed at 30 °C. Using the culture medium composed of 20 g dextrin l^?1, 40 g Tween 80 l^?1 and 30 g peptone l^?1, TliA was produced at a level of 2,200 U ml^?1 in a flask culture. The TliA production increased about 3.8-fold (8,450 U ml^?1) in batch fermentation using a 2.5 l fermentor, which was about 7.7-fold higher than that of previously reported TliA production.     

UFEIII, a fibrinolytic protease from the marine invertebrate, Urechis unicinctus

A new serine protease with fibrinolytic activity from a marine invertebrate, Urechis unicinctus, was purified to electrophoretic homogeneity using column chromatography. SDS-PAGE of the purified enzyme showed a single polypeptide chain with MW ~20.8 kDa. Its N-terminal sequence was IIGGSQAAITSY. The purified enzyme, UFEIII, was stable at pH 6–10 below 60 °C with an optimum pH of 8.5 at approx. 55 °C. The enzyme activity was significantly inhibited by PMSF and SBTI suggesting that it was a serine protease. In fibrin plate assays, UFEIII was contained 1.46 × 10³ U (urokinase units) mg^?1 total fibrinolytic activity, which consisted of 692 U mg^?1 direct fibrinolytic activity and 769 U mg^?1 plasminogen-activator activity. K_m and V_max values for azocasein were 1 mg ml^?1 and 43 μg min^?1 ml^?1, respectively.     

Heterologous expression and biochemical characterization of acetyl xylan esterase from Coprinopsis cinerea

Acetyl xylan esterase (AXE) from basidiomycete Coprinopsis cinerea Okayama 7 (#130) was functionally expressed in Pichia pastoris with a C-terminal tag under the alcohol oxidase 1 (AOX1) promoter and secreted into the medium at 1.5 mg l^?1. Its molecular mass was estimated to be 65.5 kDa based on the SDS-PAGE analysis, which is higher than the calculated molecular mass of 40 kDa based on amino acid composition. In-silico analysis of the amino acid sequence predicted two potential N-glycosylation sites. Results from PNGase F deglycosylation and mass spectrum confirmed the presence of N-glycosylation on the recombinant AXE with predominant N-glycans HexNAc₂Hex_9–16. The recombinant AXE showed best activity at 40 °C and pH 8. It showed not only acetyl esterase activity with a K_m of 4.3 mM and a V_max of 2.15 U mg^?1 for hydrolysis of 4-nitrophenyl acetate but also a butyl esterase activity for hydrolysis of 4-nitrophenyl butyrate with a K_m of 0.11 mM and V_max of 0.78 U mg^?1. The presence of two additional amino acid residues at its native N-terminus was found to help stabilize the enzyme against the protease cleavages without affecting its activity.     

Oxygen transfer as a tool for fine-tuning recombinant protein production by <Emphasis Type="Italic">Pichia pastoris</Emphasis> under glyceraldehyde-3-phosphate dehydrogenase promoter

Effects of oxygen transfer on recombinant protein production by Pichia pastoris under glyceraldehyde-3-phosphate dehydrogenase promoter were investigated. Recombinant glucose isomerase was chosen as the model protein. Two groups of oxygen transfer strategies were applied, one of which was based on constant oxygen transfer rate where aeration rate was Q _O/V = 3 and 10 vvm, and agitation rate was N = 900 min^?1; while the other one was based on constant dissolved oxygen concentrations, C _DO = 5, 10, 15, 20 and 40 % in the fermentation broth, by using predetermined exponential glucose feeding with μ _o = 0.15 h^?1. The highest cell concentration was obtained as 44 g L^?1 at t = 9 h of the glucose fed-batch phase at C _DO = 20 % operation while the highest volumetric and specific enzyme activities were obtained as 4440 U L^?1 and 126 U g^?1 cell, respectively at C _DO = 15 % operation. Investigation of specific enzyme activities revealed that keeping C _DO at 15 % was more advantageous with an expense of relatively higher by-product formation and lower specific cell growth rate. For this strategy, the highest oxygen transfer coefficient and oxygen uptake rate were K _L a = 0.045 s^?1 and OUR = 8.91 mmol m^?3 s^?1, respectively.     

Heterologous expression of β-xylosidase gene from Paecilomyces thermophila in Pichia pastoris

β-xylosidase from thermophilic fungi Paecilomyces thermophila was functionally expressed in Pichia pastoris with a his tag in the C-terminal under the alcohol oxidase 1 (AOX1) promoter and secreted into the medium at 0.22 mg l^?1. Its molecular mass was estimated to be 52.3 kDa based on the SDS-PAGE analysis, which is 1.3 times higher than the predicted 39.31 kDa from its amino acid compositions, although no potential N- or O- glycosylation sites were predicted from its amino acid sequence. This is presumed to be caused by some unpredictable posttranslational modifications based on mass spectrum analysis of the recombinant protein. The enzyme was most active at 60 °C and pH 7. It showed not only a β-xylosidase activity with a K_m of 8 mM and a V_max of 54 μmol min^?1 mg^?1 for hydrolysis of p-nitrophenyl β-d-xylopyranoside but also an arabinofuranosidase activity (6.2 U mg^?1) on p-nitrophenyl arabinofuranoside.     

Characterization and application of a newly synthesized 2-deoxyribose-5-phosphate aldolase

A codon-optimized 2-deoxyribose-5-phosphate aldolase (DERA) gene was newly synthesized and expressed in Escherichia coli to investigate its biochemical properties and applications in synthesis of statin intermediates. The expressed DERA was purified and characterized using 2-deoxyribose-5-phosphate as the substrate. The specific activity of recombinant DERA was 1.8 U/mg. The optimum pH and temperature for DERA activity were pH 7.0 and 35 °C, respectively. The recombinant DERA was stable at pH 4.0–7.0 and at temperatures below 50 °C. The enzyme activity was inhibited by 1 mM of Ni²⁺, Ba²⁺ and Fe²⁺. The apparent K _m and V _max values of purified enzyme for 2-deoxyribose-5-phosphate were 0.038 mM and 2.9 μmol min^?1 mg^?1, for 2-deoxyribose were 0.033 mM and 2.59 μmol min^?1 mg^?1, respectively, which revealed that the enzyme had similar catalytic efficiency towards phosphorylated and non-phosphorylated substrates. To synthesize statin intermediates, the bioconversion process for production of (3R, 5S)-6-chloro-2,4,6-trideoxyhexose from chloroacetaldehyde and acetaldehyde by the recombinant DERA was developed and a conversion of 94.4 % was achieved. This recombinant DERA could be a potential candidate for application in production of (3R, 5S)-6-chloro-2,4,6-trideoxyhexose.     

Subcellular Localization and Kinetic Characterization of a Gill (Na+, K+)-ATPase from the Giant Freshwater Prawn Macrobrachium rosenbergii

The stimulation by Mg²⁺, Na⁺, K⁺, NH₄ ⁺, and ATP of (Na⁺, K⁺)-ATPase activity in a gill microsomal fraction from the freshwater prawn Macrobrachium rosenbergii was examined. Immunofluorescence labeling revealed that the (Na⁺, K⁺)-ATPase α-subunit is distributed predominantly within the intralamellar septum, while Western blotting revealed a single α-subunit isoform of about 108 kDa M _r. Under saturating Mg²⁺, Na⁺, and K⁺ concentrations, the enzyme hydrolyzed ATP, obeying cooperative kinetics with V _M = 115.0 ± 2.3 U mg^?1, K _0.5 = 0.10 ± 0.01 mmol L^?1. Stimulation by Na⁺ (V _M = 110.0 ± 3.3 U mg^?1, K _0.5 = 1.30 ± 0.03 mmol L^?1), Mg²⁺ (V _M = 115.0 ± 4.6 U mg^?1, K _0.5 = 0.96 ± 0.03 mmol L^?1), NH₄ ⁺ (V _M = 141.0 ± 5.6 U mg^?1, K _0.5 = 1.90 ± 0.04 mmol L^?1), and K⁺ (V _M = 120.0 ± 2.4 U mg^?1, K _M = 2.74 ± 0.08 mmol L^?1) followed single saturation curves and, except for K⁺, exhibited site–site interaction kinetics. Ouabain inhibited ATPase activity by around 73 % with K _I = 12.4 ± 1.3 mol L^?1. Complementary inhibition studies suggest the presence of F₀F₁–, Na⁺-, or K⁺-ATPases, but not V(H⁺)- or Ca²⁺-ATPases, in the gill microsomal preparation. K⁺ and NH₄ ⁺ synergistically stimulated enzyme activity (≈25 %), suggesting that these ions bind to different sites on the molecule. We propose a mechanism for the stimulation by both NH₄ ⁺, and K⁺ of the gill enzyme.     

Enhanced expression of endoinulinase from Aspergillus niger by codon optimization in Pichia pastoris and its application in inulooligosaccharide production

In the present study, the endoinulinase gene (EnInu) from Aspergillus niger CICIM F0620 was optimized according to the codon usage of Pichia pastoris and both the native and the optimized gene were expressed in P. pastoris. Use of the optimized gene resulted in the secretion of recombinant endoinulinase activity that reached 1,349 U ml^?1, 4.18 times that observed using the native gene. This is the highest endoinulinase activity reported to date. The recombinant enzyme was optimally active at pH 6.0 and 60 °C. Moreover, inulooligosaccharides production from inulin was studied using the recombinant enzyme produced from the optimized gene. After 8 h under optimal conditions, which included 400 g l^?1 inulin, an enzyme concentration of 40 U g^?1 substrate, 50 °C and pH 6.0, the inulooligosaccharide yield was 91 %. The high substrate concentration and short reaction time described here should reduce production costs distinctly, compared with the conditions used in previous studies. Thus, this study may provide the basis for the industrial use of this recombinant endoinulinase for the production of inulooligosaccharides.     

Characterization and constitutive expression of a novel endo-1,4-β-d-xylanohydrolase from Aspergillus niger in Pichia pastoris

A putative endo-1,4-β-d-xylanohydrolase gene xyl10 from Aspergillus niger, encoding a 308-residue mature xylanase belonging to glycosyl hydrolase family 10, was constitutively expressed in Pichia pastoris. The recombinant Xyl10 exhibited optimal activity at pH 5.0 and 60 °C with more than 50 % of the maximum activity from 40 to 70 °C. It retained more than 90 % of the original activity after incubation at 60 °C (pH 5.0) for 30 min and more than 74 % after incubation at pH 3.0–13.0 for 2 h (25 °C). The specific activity, K _m and V _max values for purified Xyl10 were, respectively, 3.2 × 10³ U mg^?1, 3.6 mg ml^?1 and 5.4 × 10³ μmol min^?1 mg^?1 towards beechwood xylan. The enzyme degraded xylan to a series of xylooligosaccharides and xylose. The recombinant enzyme with these properties has the potential for various industrial applications.     

Characterization and expression of glucosamine-6-phosphate synthase from Saccharomyces cerevisiae in Pichia pastoris

Glucosamine-6-phosphate (GlcN-6-P) synthase from Saccharomyces cerevisiae was expressed in Pichia pastoris SMD1168 GIVING maximum activity of 96 U ml^?1 for the enzyme in the culture medium. By SDS-PAGE, the enzyme, a glycosylated protein, had an apparent molecular mass of 90 kDa. The enzyme was purified by gel exclusion chromatography to near homogeneity, with a 90 % yield and its properties were characterized. Optimal activities were at pH 5.5 and 55 °C, respectively, at which the highest specific activity was 6.8 U mg protein ^?1. The enzyme was stable from pH 4.5 to 5.5 and from 45 to 60 °C. The K_m and V_max of the GlcN-6-P synthase towards d-fructose 6-phosphate were 2.8 mM and 6.9 μmol min^?1 mg^?1, respectively.     

Optimization of the production of Aspergillus niger α-glucosidase expressed in Pichia pastoris

The α-glucosidase (AGL) from Aspergillus niger has been applied to produce isomaltooligosaccharides. In the present study, various factors which affect the yield of recombinant AGL, produced by engineered Pichia pastoris, were investigated. The expression level reached 5.5 U ml^?1 in bioreactor after optimization of parameters of initial induction cell density, induction temperature and methanol concentration. In addition, it was found that coexpression of protein disulfide isomerase (PDI) inhibited the growth of the engineered P. pastoris strains and had an adverse effect on the production of AGL, while codon optimization of native A. niger α-glucosidase encoding gene (aglu) resulted in a significant enhancement of enzyme production, which reached 10.1 U ml^?1. We believe that yield of AGL is increased by codon optimization as a result of enhanced translation efficiency as well as more stable mRNA secondary structure. In contrast, PDI coexpression under the control of alcohol oxidase promoter (PAOX1) seems to be less efficient in helping disulfide bond formation in AGL while probably induce unfolded protein response, which further leads to cell apoptosis and increased protein degradation.     

High-level extracellular production of d-Psicose-3-epimerase with recombinant Escherichia coli by a two-stage glycerol feeding approach

The aim of this study is to achieve high-level extracellular production of d-Psicose-3-epimerase (DPE) with recombinant Escherichia coli. High-level production of DPE is one of the key factors in d-Psicose production. In the present study, the gene AAL45544.1 from Agrobacterium tumefaciens str. C58 was modified by artificial synthesis for overexpression in E. coli. The total DPE activity reached 3.96 U mL^?1 after optimization of the media composition, induction temperature, and concentration of inducer. Furthermore, it was found that addition of glycine had a positive effect on the extracellular production of DPE, which reached 3.5 U mL^?1. Finally, a two-stage glycerol feeding strategy based on both the specific growth rate before induction and the amount of glycerol residues after induction was applied in a 3-L fermenter. After a series of optimal strategies in the 3-L fermenter, the total and extracellular DPE activity were 5.08- and 3.11-fold higher than that noted in the shake flask. The extracellular and intracellular DPE activity reached 10.9 and 13.2 U mL^?1, achieving 25.5 and 31.1 % conversion of d-fructose to d-psicose, respectively. The systemic strategies presented in this study provide valuable novel information for the industrial application of DPE.     

Production of cyclodextrin glycosyltransferase by immobilized <Emphasis Type="Italic">Bacillus</Emphasis> sp. on chitosan matrix

The whole-cell immobilization on chitosan matrix was evaluated. Bacillus sp., as producer of CGTase, was grown in solid-state and batch cultivation using three types of starches (cassava, potato and cornstarch). Biomass growth and substrate consumption were assessed by flow cytometry and modified phenol–sulfuric acid assays, respectively. Qualitative analysis of CGTase production was determined by colorless area formation on solid culture containing phenolphthalein. Scanning electron microscopy (SEM) analysis demonstrated that bacterial cells were immobilized on chitosan matrix efficiently. Free cells reached very high numbers during batch culture while immobilized cells maintained initial inoculum concentration. The maximum enzyme activity achieved by free cells was 58.15 U ml^?1 (36 h), 47.50 U ml^?1 (36 h) and 68.36 U ml^?1 (36 h) on cassava, potato and cornstarch, respectively. CGTase activities for immobilized cells were 82.15 U ml^?1 (18 h) on cassava, 79.17 U ml^?1 (12 h) on potato and 55.37 U ml^?1 (in 6 h and max 77.75 U ml^?1 in 36 h) on cornstarch. Application of immobilization technique increased CGTase activity significantly. The immobilized cells produced CGTase with higher activity in a shorter fermentation time comparing to free cells.     

Production of tartaric acid using immobilized recominant <Emphasis Type="Italic">cis</Emphasis>-epoxysuccinate hydrolase

Objective

To investigate the expression and immobilization of recombinant cis-epoxysuccinate hydrolase (ESH), and its application in the biological production of l-(+)-tartaric acid.

Results

E. coli BL21 (DE3)/pET11a-ESH (His) was engineered to express recombinant ESH. The enzyme had an activity of 262 U mg^?1. The recombinant ESH was immobilized on agarose Ni-IDA matrix with metal ion affinity interaction to improve its thermostability and pH stability. The immobilization efficiency and activity yield were 94 and 95%, respectively. The specific catalytic efficiency of immobilized ESH was 104 mg U^?1 h^?1 during the continuous enzymatic production process.

Conclusion

ESH with a histidine tag was immobilized and used for the continuous production of l-(+)-tartaric acid.

     

Influence of process temperature on recombinant enzyme activity in Escherichia coli fed-batch cultures

The influence of proteolysis over recombinant protein quality has been studied using rhamnulose 1-phosphate aldolase (RhuA) production as case example. Progressive induction by means of continuous isopropyl-β-d-thiogalactopyranoside (IPTG) dosage in Escherichia coli fed-batch cultures led to high specific levels of recombinant protein. However, the specific activity profile did not correlate to the specific protein content when the process was run at 37 °C and there was a decrease of the enzyme activity along the induction phase. Specific activity loss depending on the presence of an energy source was observed at short term, but protein degradation due to the action of energy-independent metalloproteases occurred after a longer time period. The effects of lowering the temperature were analysed on both mechanisms, and a reduction of the specific activity loss was observed when the process temperature was decreased to 28 °C. Lower plasmid copy number and specific production rates probably alleviated the metabolic load on host cell during recombinant protein overexpression, and a high increase of the enzyme activity was achieved in high cell density fed-batch cultures under these conditions.     

Characterization of a newly synthesized carbonyl reductase and construction of a biocatalytic process for the synthesis of ethyl (S)-4-chloro-3-hydroxybutanoate with high space-time yield

A carbonyl reductase (SCR2) gene was synthesized and expressed in Escherichia coli after codon optimization to investigate its biochemical properties and application in biosynthesis of ethyl (S)-4-chloro-3-hydroxybutanoate ((S)-CHBE), which is an important chiral synthon for the side chain of cholesterol-lowering drug. The recombinant SCR2 was purified and characterized using ethyl 4-chloro-3-oxobutanoate (COBE) as substrate. The specific activity of purified enzyme was 11.9 U mg^?1. The optimum temperature and pH for enzyme activity were 45 °C and pH 6.0, respectively. The half-lives of recombinant SCR2 were 16.5, 7.7, 2.2, 0.41, and 0.05 h at 30 °C, 35 °C, 40 °C, 45 °C, and 50 °C, respectively, and it was highly stable in acidic environment. This SCR2 displayed a relatively narrow substrate specificity. The apparent K _m and V _max values of purified enzyme for COBE are 6.4 mM and 63.3 μmol min^?1 mg^?1, respectively. The biocatalytic process for the synthesis of (S)-CHBE was constructed by this SCR2 in an aqueous–organic solvent system with a substrate fed-batch strategy. At the final COBE concentration of 1 M, (S)-CHBE with yield of 95.3 % and e.e. of 99 % was obtained after 6-h reaction. In this process, the space-time yield per gram of biomass (dry cell weight, DCW) and turnover number of NADP⁺ to (S)-CHBE were 26.5 mmol L^?1 h^?1 g^?1 DCW and 40,000 mol/mol, respectively, which were the highest values as compared with other works.