Industrial scale of optimization for the production of carboxymethylcellulase from rice bran by a marine bacterium, Bacillus subtilis subsp. subtilis A-53

Rice bran and yeast extract were found to be the best combination of carbon and nitrogen sources for the production of carboxymethycellulase (CMCase) by Bacillus subtilis subsp. subtlis A-53. Optimal concentrations of rice bran and yeast extract for the production of CMCase were 5.0% (w/v) and 0.10% (w/v), respectively. Optimal temperature and initial pH of medium for cell growth of B. subtilus subsp. subtilis A-53 were 35 °C and 7.3, whereas those for the production of CMCase by B. subtilus subsp. subtilis A-53 were 30 °C and 6.8. Optimal agitation speed and aeration rate in a 7 L bioreactor were 300 rpm and 1.0 vvm, respectively. The optimal agitation speed and aeration rate for the production of CMCase by B. subtilus subsp. subtilis A-53 were lower than those for cell growth. The highest productions of CMCase by B. subtilus subsp. subtilis A-53 in 7 and 100 L bioreactors were 150.3 and 196.8 U mL⁻¹, respectively.     

Enhanced Production of carboxymethylcellulase by a marine bacterium,Bacillus velezensis A-68, by using rice hulls in pilot-scale bioreactor under optimized conditions for dissolved oxygen

The optimal conditions for the production of carboxymethylcellulase (CMCase) by Bacillus velezensis A-68 at a flask scale have been previously reported. In this study, the parameters involved in dissolved oxygen in 7 and 100 L bioreactors were optimized for the pilot-scale production of CMCase. The optimal agitation speed and aeration rate for cell growth of B. velezensis A-68 were 323 rpm and 1.46 vvm in a 7 L bioreactor, whereas those for the production of CMCase were 380 rpm and 0.54 vvm, respectively. The analysis of variance (ANOVA) implied that the highly significant factor for cell growth was the aeration rate, whereas that for the production of CMCase was the agitation speed. The optimal inner pressures for cell growth and the production of CMCase by B. velezensis A-68 in a 100 L bioreactor were 0.00 and 0.04 MPa, respectively. The maximal production of CMCase in a 100 L bioreactor under optimized conditions using rice hulls was 108.1 U/ml, which was 1.8 times higher than that at a flask scale under previously optimized conditions.     

Purification and characterization of carboxymethylcellulase isolated from a marine bacterium, Bacillus subtilis subsp. subtilis A-53

The microorganism hydrolyzing carboxymethylcellulose (CMC) was isolated from seawater, identified as Bacillus subtilis subsp. subtilis by analyses of 16S rDNA and partial sequences of the gyrA gene, and named as B. subtilis subsp. subtilis A-53. The molecular weight of the purified carboxymethylcellulase (CMCase) was estimated to be about 56 kDa with the analysis of SDS-PAGE. The purified CMCase hydrolyzed carboxymethylcellulose (CMC), cellobiose, filter paper, and xylan, but not avicel, cellulose, and p-nitrophenyl-β-d-glucospyranoside (PNPG). Optimal temperature and pH for the CMCase activity were determined to be 50 °C and 6.5, respectively. More than 70% of original CMCase activity was maintained at relative low temperatures ranging from 20 to 40 °C after 24 h incubation at 50 °C. The CMCase activity was enhanced by EDTA and some metal ions in order of EDTA, K⁺, Ni²⁺, Sr²⁺, Pb²⁺, and Mn²⁺, but inhibited by Co²⁺ and Hg²⁺.     

Comparison of optimal conditions for mass production of carboxymethylcellulase by <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/A-68 with other recombinants in pilot-scale bioreactor

The optimal conditions for mass production of carboxymethylcellulase (CMCase) by E. coli JM109/A-68 were investigated and compared with other E. coli JM109 recombinants producing CMCase. The optimal agitation speed and aeration rate for cell growth of E. coli JM109/A- 68 were 500 rpm and 0.50 vvm in a 7 L bioreactor, whereas those for production of CMCase were 416 rpm and 0.95 vvm. The optimal vessel pressures for cell growth as well as production of CMCase in a 100 L bioreactor were 0.04 MPa. The maximal production of CMCase by E. coli JM109/A-68 under the optimized conditions in a 100 L bioreactor was 11.0 times higher than its wild type, B. velezensis A-68. Optimal conditions for mass production of CMCase by recombinants were different from those for wild strains. The higher production of CMCase by E. coli JM109/A-68 and other recombinant of E. coli seemed to result from its higher cell growth under the optimal conditions for dissolved oxygen and its mixed-growth associated production pattern compared to the growthassociated production of B. velezensis A-68.     

Construction of a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/A-68 for production of carboxymethylcellulase and comparison of its production with its wild type, <Emphasis Type="Italic">Bacillus velezensis</Emphasis> A-68 in a pilot-scale bioreactor

A gene encoding carboxymethylcellulase (CMCase) of Bacillus velezensis A-68 had been cloned in Escherichia coli JM109. Based on productivity and economic aspect, rice bran and ammonium chloride were chosen to be optimal carbon and nitrogen sources for production of CMCase by E. coli JM109/A-68. The optimal conditions for rice bran, ammonium chloride, and initial pH of medium for production of CMCase were established by the response surface methodology (RSM). The concentrations of four salts in the medium, K₂HPO₄, NaCl, MgSO₄·7H₂O, and (NH₄)₂SO₄, for production of CMCase also were optimized. The optimal temperatures for cell growth and production of CMCase were 37°C. The maximal production of CMCase by E. coli JM109/A-68 was 880.2 U/mL, which was 10.5 time higher than its wild type, B. velezensis A-68. The production of CMCase by E. coli JM109/A-68 was compared with that by B. velezensis A-68 in a 100 L pilot-scale bioreactor under the optimized conditions. The production of CMCase by E. coli JM109/A-68 was found to be the mixed-growth associated unlike the growthassociated production of CMCase by B. velezensis A-68.     

Enhanced production of penicillin G acylase from a recombinant Escherichia coli

Penicillin G acylase (pac) gene was cloned into a stable asd ⁺ vector (pYA292) and expressed in Escherichia coli. This recombinant strain produced 1000 units penicillin G acylase g^–1 cell dry wt, which is 23-fold more than that produced by parental Escherichia coli ATCC11105. This enzyme was purified to 16 units mg^–1 protein by a novel two-step process.     

Enhanced plasmid stability and production of hEGF by immobilized recombinant E. coli JM101

Recombinant Escherichia coli JM101 was immobilized with porous polyurethane foam (PUF) particle as supporter matrix for human epidermal growth factor (hEGF) production. Flask culture showed that cell immobilization in PUF can improve cell growth and hEGF expression. A bubble column and a three-phase fluidized bed bioreactor by self-design was further applied to produce hEGF, respectively. The results demonstrated that PUF is a feasible immobilized supporter material with good biocompatibility. Immobilization could also decrease the probability for segregational plasmid loss and overgrowth of plasmid-free cells. Cell density, plasmid stability and hEGF productivity were higher than those without the foam matrix, respectively. hEGF productivity was enhanced from 8.73 mg/l h of free-culture to 11.4 mg/l h of immobilized cultivation.     

Characterization of the Bacillus subtilis WL-3 mannanase from a recombinant Escherichia coli

A mannanase was purified from a cell-free extract of the recombinant Escherichia coli carrying a Bacillus subtilis WL-3 mannanase gene. The molecular mass of the purified mannanase was 38 kDa as estimated by SDS-PAGE. Optimal conditions for the purified enzyme occurred at pH 6.0 and 60 degrees C. The specific activity of the purified mannanase was 5,900 U/mg on locust bean gum (LBG) galactomannan at pH 6.0 and 50 degrees C. The activity of the enzyme was slightly inhibited by Mg(2+), Ca(2+), EDTA and SDS, and noticeably enhanced by Fe(2+). When the enzyme was incubated at 4 degrees C for one day in the presence of 3 mM Fe(2+), no residual activity of the mannanase was observed. The enzyme showed higher activity on LBG and konjac glucomannan than on guar gum galactomannan. Furthermore, it could hydrolyze xylans such as arabinoxylan, birchwood xylan and oat spelt xylan, while it did not exhibit any activities towards carboxymethylcellulose and para-nitrophenyl-beta-mannopyranoside. The predominant products resulting from the mannanase hydrolysis were mannose, mannobiose and mannotriose for LBG or mannooligosaccharides including mannotriose, mannotetraose, mannopentaose and mannohexaose. The enzyme could hydrolyze mannooligosaccharides larger than mannobiose.     

Statistical optimization for production of carboxymethylcellulase of <Emphasis Type="Italic">Bacillus amyloliquefaciens</Emphasis> DL-3 by a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/DL-3 from rice bran using response surface method

The optimal conditions for production of carboxymethylcellulase (CMCase) of Bacillus amyloliquefaciens DL-3 by a recombinant Escherichia coli JM109/DL-3 were established at a flask scale using the response surface method (RSM). The optimal conditions of rice bran, tryptone, and initial pH of the medium for cell growth extracted by Design Expert Software were 66.1 g/L, 6.2 g/L, and 7.2, respectively, whereas those for production of CMCase were 58.0 g/L, 5.0 g/L, and 7.1. The analysis of variance (ANOVA) of results from central composite design (CCD) indicated that significant factor (“probe > F” less than 0.0500) for cell growth was rice bran, whereas those for production of CMCase were rice bran and initial pH of the medium. The optimal temperatures for cell growth and the production of CMCase by E. coli JM109/DL-3 were found to be 37°C. The optimal agitation speed and aeration rate of 7 L bioreactors for cell growth were 498 rpm and 1.4 vvm, whereas those for production of CMCase were 395 rpm and 1.1 vvm. The ANOVA of results indicated that the aeration rate was more significant factor (“probe > F” less than 0.0001) than the agitation speed for cell growth and production of CMCase. The optimal inner pressure for cell growth was 0.08 MPa, whereas that for the production of CMCase was 0.06 MPa. The maximal production of CMCase by E. coli JM109/DL-3 under optimized conditions was 871.0 U/mL, which was 3.0 times higher than the initial production of CMCase before optimization.     

基因工程菌大肠杆菌JM109富集废水中镍离子的研究

利用通过基因工程技术所构建的在细胞内同时表达出高特异性镍转运蛋白和金属硫蛋白的基因工程菌富集水体中的镍离子。菌体细胞对Ni²⁺的富集速率很快,富集过程满足Langmuir等温线模型。与原始宿主菌相比,经基因改造的基因工程菌不仅最大镍富集容量增加了5倍多,而且对pH值、离子强度的变化及其它共存重金属离子的影响都呈现出更强的适应性。相比而言,Na⁺、Ca²⁺、Cd²⁺、Pb²⁺的影响较小,但Mg²⁺、Hg²⁺和Cu²⁺所引起的负面效应较大。进一步的实验表明基因工程菌对Ni2+的富集行为不需要外加营养物质。     

Effect of glucose supply strategy on acetate accumulation, growth, and recombinant protein production by Escherichia coli BL21 (lambdaDE3) and Escherichia coli JM109

Two Escherichia coli strains, widely used for the production of various recombinant proteins, were compared for their pre-induction growth and acetate accumulation patterns. The strains studied were E. coli BL21 (lambdaDE3), transformed with a plasmid encoding Pseudomonas exotoxin A, and an E. coli K12 derived strain, JM109, carrying a plasmid encoding maltose-binding protein fused with HIV protease. Cultures were grown in controlled bench-top fermentors to the optimal pre-induction density in both high glucose batch and low glucose fed batch strategies. The results showed the superiority of E. coli BL21 (lambdaDE3) as a host for a recombinant protein expression system. For example, JM109 responds differently to high glucose concentration and to low glucose concentration. Its acetate concentration was as high as 10 g/L in a batch mode and 5 g/L in a fed batch mode. In comparison, strain BL21 (lambdaDE3) reached 2 g/L acetate when grown in batch mode and not more than 1 g/L acetate when grown in a fed batch mode. E. coli BL21 (lambdaDE3), most likely, possesses an acetate self-control mechanism which makes it possible to grow to the desired pre-induction density in a high glucose medium using simple batch propagation techniques. Such a technique is cost effective, reproducible, and easy to scale up. (c) 1996 John Wiley & Sons, Inc.     

Vanillin bioproduction from alkaline hydrolyzate of corn cob by Escherichia coli JM109/pBB1

Hydrolysis of corn cob performed for 6 h with 0.5 N NaOH at solid/liquid ratio of 0.084 g/g allowed obtaining a hydrolyzate containing 1171 ± 34 mg/l ferulic acid and 2156 ± 63 mg/l p-coumaric acid that was used as a medium for vanillin bioproduction by the engineered strain Escherichia coli JM109/pBB1. Aiming at maximizing vanillin bioproduction, the effects of medium heat sterilization, one-stage or two-stage pre-cultivation, adaptation of the microorganism to the hydrolyzate and inoculum biomass level were investigated. Biomass pre-cultivated once in unsterilized hydrolyzate was able to effectively convert ferulic and p-coumaric acids to a mixture of vanillin, vanillic acid and vanillyl alcohol provided with the typical vanilla flavor. At initial biomass concentration of 0.5 g_DM/l, maximum values of vanillin concentration (239 ± 15 mg/l), vanillin yield on consumed ferulic acid (0.66 ± 0.03 mol/mol) and vanillin volumetric productivity (10.9 ± 0.7 mg/lh) were obtained after 22 h.     

Enhanced secretion of Escherichia coli beta-lactamase by a spontaneous erythromycin-resistant mutant of Bacillus subtilis

An extracellular-protease-deficient mutant, ME142, was isolated from Bacillus subtilis as a spontaneous erythromycin-resistant (Eryr) clone. This mutant showed conditional sporulation and only sporulated normally in the absence of erythromycin. In the presence of the antibiotic, sporulation was greatly reduced. Production of extracellular proteases by ME142 also exhibited conditional deficiency, possibly due to pleiotropic effects of the sporulation deficiency. The production of protease was 2-10% that of the wild-type level in the presence of erythromycin. ME142 showed poor competence for transformation even in the absence of erythromycin; however, derivatives of ME142 were isolated which had the same Eryr phenotype but which exhibited normal competence. One such mutant, ME162, was used as a host for the secretion of Escherichia coli beta-lactamase. The amount of beta-lactamase in the culture supernatants of ME162 increased significantly when the cells were cultured with erythromycin, suggesting that proteolysis of the beta-lactamase in the supernatants of ME162 was greatly reduced as compared to that in the supernatants of the wild-type strain.     

Regioselective biooxidation of (+)-valencene by recombinant E. coli expressing CYP109B1 from Bacillus subtilis in a two-liquid-phase system

Background  

(+)-Nootkatone (4) is a high added-value compound found in grapefruit juice. Allylic oxidation of the sesquiterpene (+)-valencene (1) provides an attractive route to this sought-after flavoring. So far, chemical methods to produce (+)-nootkatone (4) from (+)-valencene (1) involve unsafe toxic compounds, whereas several biotechnological approaches applied yield large amounts of undesirable byproducts. In the present work 125 cytochrome P450 enzymes from bacteria were tested for regioselective oxidation of (+)-valencene (1) at allylic C2-position to produce (+)-nootkatone (4) via cis- (2) or trans-nootkatol (3). The P450 activity was supported by the co-expression of putidaredoxin reductase (PdR) and putidaredoxin (Pdx) from Pseudomonas putida in Escherichia coli.     

Large-scale production and characterization of Bacillus thuringiensis subsp. tenebrionis insecticidal protein from Escherichia coli

Bacillus thuringiensis subsp. tenebrionis insecticidal protein was produced in recombinant Escherichia coli and purified to near homogeneity to provide quantities of protein for safety-assessment studies associated with the registration of transgenic potato plants. The 68-kDa protein is produced naturally by Bacillus thuringiensis subsp. tenebrionis by translation initiation at an internal initiation site in the native DNA sequence. The gene sequence specific for this truncated protein was expressed in E. coli strain JM 101 and fermented at the 1000-l scale. The protein accumulated as insoluble inclusion bodies, and was purified by extraction at pH␣10.8 with carbonate buffer, selective precipitation at pH 9.0, and differential centrifugation. No chromatography steps were required to produce over 50 g purified protein as a lyophilized powder with a purity greater than 95 % and demonstrating full insecticidal activity against Colorado potato beetle larvae. The protein was further characterized to assure identity and suitability for use in safety-assessment studies. Received: 31 May 1996 / Received revision: 11 September 1996 / Accepted: 13 October 1996     

Overexpression of a recombinant wild-type and His-tagged Bacillus subtilis glycine oxidase in Escherichia coli.

We have cloned the gene coding for the Bacillus subtilis glycine oxidase (GO), a new flavoprotein that oxidizes glycine and sarcosine to the corresponding alpha-keto acid, ammonia and hydrogen peroxide. By inserting the DNA encoding for GO into the multiple cloning site of the expression vector pT7.7 we produced a recombinant plasmid (pT7-GO). The pT7-GO encodes a fully active fusion protein with six additional residues at the N-terminus of GO (MARIRA). In BL21(DE3)pLysS Escherichia coli cells, and under optimal isopropyl thio-beta-D-galactoside induction conditions, soluble and active chimeric GO was expressed up to 1.14 U g(-1) of cell (and a fermentation yield of 3.82 U x L(-1) of fermentation broth). An N-terminal His-tagged protein (HisGO) was also successfully expressed in E. coli as a soluble protein and a fully active holoenzyme. HisGO represents approximately 3.9% of the total soluble protein content of the cell. The His-tagged GO was purified in a single step by nickel-chelate chromatography to a specific activity of 1.06 U x mg(-1) protein at 25 degrees C and with a yield of 98%. The characterization of the purified enzyme showed that GO is a homotetramer of approximately 180 kDa with the spectral properties typical of flavoproteins. GO exhibits good thermal stability, with a Tm of 46 degrees C after 30 min incubation; its stability is maximal in the 7.0-8.5 pH range. A comparison of amino-acid sequence and substrate specificity indicates that GO has similarities to other flavoenzymes acting on primary amines and on D-amino acids.     

Enhanced production of recombinant proteins in Escherichia coli by filamentation suppression

During growth of high-cell-density cultures of Escherichia coli, overproduction of recombinant proteins often results in increased stress response, cell filamentation, and growth cessation. Filamentation of cells consequently lowers final achievable cell concentration and productivity of the target protein. Reported here is a methodology that should prove useful for the enhancement of cell growth and protein productivity by the suppression of cell filamentation. By the coexpression of the E. coli ftsA and ftsZ genes, which encode key proteins in cell division, growth of recombinant strains as well as production of human leptin and human insulin-like growth factor I was improved. Observation of cell morphology revealed that the coexpression of the ftsA and ftsZ genes successfully suppressed filamentation caused by the accumulation of recombinant proteins.     

Enhanced production of polyhydroxyalkanoates (PHAs) from beechwood xylan by recombinant Escherichia coli

Microbial conversion of plant biomass to value-added products is an attractive option to address the impacts of petroleum dependency. In this study, a bacterial system was developed that can hydrolyze xylan and utilize xylan-derived xylose for growth and production of polyhydroxyalkanoates (PHAs). A β-xylosidase and an endoxylanase were engineered into a P(LA-co-3HB)-producing Escherichia coli strain to obtain a xylanolytic strain. Although PHA production yields using xylan as sole carbon source were minimal, when the xylan-based media was supplemented with a single sugar (xylose or arabinose) to permit the accumulation of xylan-derived xylose in the media, PHA production yields increased up to 18-fold when compared to xylan-based production, and increased by 37 % when compared to production from single sugar sources alone. ¹H-Nuclear magnetic resonance (NMR) analysis shows higher accumulation of xylan-derived xylose in the media when xylan was supplemented with arabinose to prevent xylose uptake by catabolite repression. ¹H-NMR, gel permeation chromatography, and differential scanning calorimetry analyses corroborate that the polymers maintain physical properties regardless of the carbon source. This study demonstrates that accumulation of biomass-derived sugars in the media prior to their uptake by microbes is an important aspect to enhance PHA production when using plant biomass as feedstock.     

Enhanced cytidine production by a recombinant Escherichia coli strain using genetic manipulation strategies

Cytidine is a nucleoside molecule that is widely used as a precursor for antiviral drugs. In this study, a cytidine-producing strain Cyt18 was developed from Escherichia coli K-12 through 3-step genetic manipulation strategies. Cytidine deaminase gene (cdd) was firstly deleted from the E. coli K-12 strain to develop Cyt10. Furthermore, homoserine dehydrogenase gene (thrA) was inactivated from the Cyt10 strain to develop Cyt12, in which the intracellular aspartate concentration was expected to be increased. The recombinant plasmid pMG1105 containing an pyrB-pyrA operon from Bacillus amyloliquefaciens CYTI was constructed and was introduced into Cyt12 to obtain the Cyt18 strain. Compared to the Cyt12 strain, the cytidine production by the recombinant strain Cyt18 was increased by ~3-fold (722.9 mg/l vs. 249.3 mg/l).     

Expression of 3-ketoacyl-acyl carrier protein reductase (fabG) genes enhances production of polyhydroxyalkanoate copolymer from glucose in recombinant Escherichia coli JM109

Polyhydroxyalkanoates (PHAs) are biologically produced polyesters that have potential application as biodegradable plastics. Especially important are the short-chain-length-medium-chain-length (SCL-MCL) PHA copolymers, which have properties ranging from thermoplastic to elastomeric, depending on the ratio of SCL to MCL monomers incorporated into the copolymer. Because of the potential wide range of applications for SCL-MCL PHA copolymers, it is important to develop and characterize metabolic pathways for SCL-MCL PHA production. In previous studies, coexpression of PHA synthase genes and the 3-ketoacyl-acyl carrier protein reductase gene (fabG) in recombinant Escherichia coli has been shown to enhance PHA production from related carbon sources such as fatty acids. In this study, a new fabG gene from Pseudomonas sp. 61-3 was cloned and its gene product characterized. Results indicate that the Pseudomonas sp. 61-3 and E. coli FabG proteins have different substrate specificities in vitro. The current study also presents the first evidence that coexpression of fabG genes from either E. coli or Pseudomonas sp. 61-3 with fabH(F87T) and PHA synthase genes can enhance the production of SCL-MCL PHA copolymers from nonrelated carbon sources. Differences in the substrate specificities of the FabG proteins were reflected in the monomer composition of the polymers produced by recombinant E. coli. SCL-MCL PHA copolymer isolated from a recombinant E. coli strain had improved physical properties compared to the SCL homopolymer poly-3-hydroxybutyrate. This study defines a pathway to produce SCL-MCL PHA copolymer from the fatty acid biosynthesis that may impact on PHA production in recombinant organisms.