Influence of temperature on the production of an archaeal thermoactive alcohol dehydrogenase from Pyrococcus furiosus with recombinant Escherichia coli

The heterologous production of a thermoactive alcohol dehydrogenase (AdhC) from Pyrococcus furiosus in Escherichia coli was investigated. E. coli was grown in a fed-batch bioreactor in minimal medium to high cell densities (cell dry weight 76 g/l, OD₆₀₀ of 150). Different cultivation strategies were applied to optimize the production of active AdhC, such as lowering the cultivation temperature from 37 to 28°C, heat shock of the culture from 37 to 42°C and from 37 to 45°C, and variation of time of induction (induction at an OD₆₀₀ of 40, 80 and 120). In addition to the production of active intracellular protein, inclusion bodies were always observed. The maximal activity of 30 U/l (corresponding to 6 mg/l active protein) was obtained after a heat shock from 37 to 42°C, and IPTG induction of the adhC expression at an OD₆₀₀ of 120. Although no general rules can be provided, some of the here presented variations may be applicable for the optimization of the heterologous production of proteins in general, and of thermozymes in particular.     

Clinical grade production and characterization of a fusion protein comprised of the chemokine CCL2-ligand genetically fused to a mutated and truncated form of the Shiga A1 subunit

First generation chemokine ligand-Shiga A1 (SA1) fusion proteins (leukocyte population modulators, LPMs) were previously only obtained in small quantities due to the ribosomal inactivating protein properties of the SA1 moiety which inhibits protein synthesis in host cells. We therefore employed 4-aminopyrazolo[3,4-d]-pyrimidine, an inhibitor of Shiga A1, to allow the growth of these cells prior to induction and during the expression phase post-induction with IPTG. Scale-up allowed the production of gram quantities of clinical grade material of the lead candidate, OPL–CCL2–LPM. A manufacturing cell bank was established and used to produce OPL–CCL2–LPM in a fed-batch fermentation process. Induction of the expression of OPL–CCL2–LPM led to the production of 22.47 mg/L per OD₆₀₀ unit. The LPM was purified from inclusion bodies using solubilization, renaturation, refolding and chromatography steps. The identity and purity of the OPL–CCL2–LPM was determined using several analytical techniques. The product retained the ability of the SA1 moiety to inhibit protein synthesis as measured in a rabbit reticulocyte lysate cell-free protein synthesis assay and was cytotoxic to target cells. Binding studies established that the protein exerts its effects via CCR2, the cognate receptor for CCL2. Clinical trials in inflammatory nephropathies are planned.     

High-Level Production of Human Leptin by Fed-Batch Cultivation of Recombinant Escherichia coli and Its Purification

Human leptin is a 16-kDa (146-amino-acid) protein that is secreted from adipocytes and influences body weight homeostasis. In order to obtain high-level production of leptin, the human obese gene coding for leptin was expressed in Escherichia coli BL21(DE3) under the strong inducible T7 promoter. The recombinant leptin was produced as inclusion bodies in E. coli, and the recombinant leptin content was as high as 54% of the total protein content. For production of recombinant human leptin in large amounts, pH-stat fed-batch cultures were grown. Expression of leptin was induced at three different cell optical densities at 600 nm (OD₆₀₀), 30, 90, and 140. When cells were induced at an OD₆₀₀ of 90, the amount of leptin produced was 9.7 g/liter (37% of the total protein). After simple purification steps consisting of inclusion body isolation, denaturation and refolding, and anion-exchange chromatography, 144.9 mg of leptin that was more than 90% pure was obtained from a 50-ml culture, and the recovery yield was 41.1%.     

High-level production of a single chain antibody against anthrax toxin in Escherichia coli by high cell density cultivation

Previously, we isolated the M18 scFv, which is an affinity matured antibody against the anthrax toxin PA, and observed that its single chain antibody (scAb) form (M18 scAb) exhibited superior stability compared to the scFv. Here, we report high cell density cultivations for preparative scale production of M18 scAb in a 3.5 L fermenter. Briefly, a pH–stat feeding strategy was employed in fed-batch cultivation, and four different cell densities (OD₆₀₀ of 40, 80, 120, and 150) were examined for the induction of scAb gene expression. Among the four cell densities investigated, lower cell densities (OD₆₀₀ of 40) showed higher post-induction cell growth and production yields (665 mg/L of scAb). Even though lower solubility (51%) of scAb was achieved at lower cell density (OD₆₀₀ of 40), monomeric scAb could be purified with high purity (>95%) using simple purification procedures. The purified scAb from high cell density cultures showed biological activity equivalent to that of scAb purified from shake flask cultivation.     

Optimization of extracellular production of recombinant asparaginase in Escherichia coli in shake-flask and bioreactor

Various host–vector combinations were tested to maximize the extracellular production of recombinant asparaginase in Escherichia coli. Expression of recombinant asparaginase fused to pelB leader sequence under the inducible T7lac promoter in BLR (DE3) host cells resulted in optimum extracellular production in shake-flasks. Fed-batch studies were carried out using this recombinant strain and an exponential feeding strategy was used to maintain a specific growth rate of 0.3 h^–1. To check the effect of the time of induction on expression, cultures were induced with 1 mM isopropyl--D-thiogalactopyranoside at varying cell optical densities (OD₆₀₀: 33, 60, 90, 135). Although the specific product formation rates declined with increasing OD of induction, a maximum volumetric activity of 8.7×10⁵ units l^–1, corresponding to 5.24 g l^–1 of recombinant asparaginase, was obtained when induction was done at an OD₆₀₀ of 90. The recombinant protein was purified directly from the culture medium, using a rapid two-step purification strategy, which resulted in a recovery of 70% and a specific activity of 80% of that of the native enzyme.     

Recombinant expression, purification, and characterization of XorKII: a restriction endonuclease from Xanthomonas oryzae pv. oryzae

An endonuclease from Xanthomonas oryzae pathovar oryzae (Xoo) KACC10331, XorKII, was recombinantly produced in Escherichia coli by applying the stationary state induction method, which was necessary to prevent the unwanted lysis of E. coli cells. XorKII was purified by immobilized metal affinity chromatography on an FPLC system. The yield was 3.5 mg of XorKII per liter of LB medium. The purified recombinant XorKII showed that it recognized and cleaved to the same site as PstI. It behaved as a dimer as evidenced by the size exclusion chromatography. The specific activity of the purified XorKII was determined to be 31,300 U/mg. The enzyme activity was monitored by cleaving lambda DNA or YEp24 plasmid as substrates. The enzyme was the most active at 10 mM Tris–HCl pH 7.0, 10 mM MgCl₂, 1 mM dithiothreitol at 37 °C. XorKII was easily inactivated by heating at 65 °C for 5 min, but retained most of the original activity after incubation at 37 °C for 24 h.     

Investigation of factors influencing spore germination of Paenibacillus polymyxa ACCC10252 and SQR-21

Bioorganic fertilizer containing Paenibacillus polymyxa SQR-21 showed very good antagonistic activity against Fusarium oxysporum. To optimize the role of P. polymyxa SQR-21 in bioorganic fertilizer, we conducted a study of spore germination under various conditions. In this study, l-asparagine, glucose, fructose and K⁺ (AGFK), and sugars (glucose, fructose, sucrose, and lactose) plus l-alanine were evaluated to determine their ability to induce spore germination of two strains; P. polymyxa ACCC10252 and SQR-21. Spore germination was measured as a decrease in optical density at 600 nm. The effect of heat activation and germination temperature were important for germination of spores of both strains on AGFK in Tris–HCl. l-Alanine alone showed a slight increase in spore germination; however, fructose plus l-alanine significantly induced spore germination, and the maximum spore germination rate was observed with 10 mmol l⁻¹ l-alanine in the presence of 1 mmol l⁻¹ fructose in phosphate-buffered saline (PBS). In contrast, fructose plus l-alanine hardly induced spore germination in Tris–HCl; however, in addition of 10 mmol l⁻¹ NaCl into Tris–HCl, the percentages of OD₆₀₀ fall were increased by 19.6% and 24.3% for ACCC10252 and SQR-21, respectively. AGFK-induced spore germination was much more strict to germination temperature than that induced by fructose plus l-alanine. For both strains, fructose plus l-alanine-induced spore germination was not sensitive to pH. The results in this study can help to predict the effect of environmental factors and nutrients on spore germination diversity, which will be beneficial for bioorganic fertilizer storage and transportation to improve the P. polymyxa efficacy as biological control agent.     

Refolding by High Pressure of a Toxin Containing Seven Disulfide Bonds: Bothropstoxin-1 from <Emphasis Type="Italic">Bothrops jararacussu</Emphasis>

Aggregation is a serious obstacle for recovery of biologically active heterologous proteins from inclusion bodies (IBs) produced by recombinant bacteria. E. coli transformed with a vector containing the cDNA for Bothropstoxin-1 (BthTx-1) expressed the recombinant product as IBs. In order to obtain the native toxin, insoluble and aggregated protein was refolded using high hydrostatic pressure (HHP). IBs were dissolved and refolded (2 kbar, 16 h), and the effects of protein concentration, as well as changes in ratio and concentration of oxido-shuffling reagents, guanidine hydrochloride (GdnHCl), and pH in the refolding buffer, were assayed. A 32% yield (7.6 mg per liter of bacterial culture) in refolding of the native BthTx-1 was obtained using optimal conditions of the refolding buffer (Tris–HCl buffer, pH 7.5, containing 3 mM of a 2:3 ratio of GSH/GSSG, and 1 M GdnHCl). Scanning electron microscopy (SEM) showed that that disaggregation of part of IBs particles occurred upon compression and that the morphology of the remaining IBs, spherical particles, was not substantially altered. Dose-dependent cytotoxic activity of high-pressure refolded BthTx-1 was shown in C2C12 muscle cells.     

Expression and Characterization of Recombinant Sucrose Phosphorylase

SPase is widely used in the food, cosmetics, and pharmaceutical industries. Previously, a SPase gene was cloned from Bifidobacterium longum JCM1217 and constructed into Escherichia coli BL21. In this paper, its expression conditions were optimized. The results showed that several induction factors determined the expression efficiency of SPase. The initial cell density, IPTG concentration, and induction time and temperature significantly (p?<?0.01) affected the total protein content and activity of expressed SPase. The highest expression efficiency was obtained at an initial cell density of OD₆₀₀?=?0.5, with 0.05 mM IPTG, followed by shaking at 180 rpm and incubation at 30 °C for 15 h. The purified SPase had a specific activity of 122.1 U/mg, which was raised by 1.85 -fold more than that before optimization, and its recovery yield was 86%. Furthermore, SPase also showed higher thermostability. The results of this study provide essential information for the industrial production of SPase.     

Sulfate Ion Effect on Stability and Regulatory Properties of PEP Carboxylase from the C4Plant Cynodon dactylon

When Tris–SO₄was used as an extraction buffer for phosphoenolpyruvate carboxylase (PEPC) from leaves of the C₄plant Cynodon dactylon(L.) Pers., a higher extractable activity was obtained as compared to Tris–HCl, especially at low phosphoenolpyruvate concentrations and an assay pH of 7.2. The Tris–SO₄-extracted PEPC activity was stable under dilution and remained unchanged for at least 24 h at 22°C. This enzyme was less sensitive to both activation by glucose-6-phosphate and inhibition by L-malate. The effects of Tris–SO₄could be attributed to its preferential exclusion from the enzymic protein domain and, therefore, to a shifting of this oligomeric enzyme to a more aggregable form that is more stable and active.     

A型产气荚膜梭菌α毒素基因表达及其免疫保护作用的初步研究

利用PCR技术,从A型产气荚膜梭菌标准株染色体DNA中扩增出α毒素基因,构建了含α毒素基因的重组菌株BL21(DE3)(pXETA02)。经酶切鉴定和序列测定证实,构建的表达质粒pXETA02含有α毒素基因序列。经SDS-PAGE、Western blot分析和ELISA检测,重组菌株表达的α毒素蛋白能够被α毒素单抗识别。表达优化结果表明,以IPTG为诱导剂诱导α毒素表达的优化条件是:培养基pH 7.5,培养温度37℃,IPTG浓度0.8mmol/L,菌体生长密度OD600达到0.8时加入IPTG,诱导时间5h,此时α毒素蛋白表达量为34.83%。以乳糖为诱导剂诱导α毒素表达的优化条件是:培养基pH7.5、培养温度37℃,乳糖浓度0.1g/L,菌体生长密度OD600达到0.8时加入乳糖,诱导时间5h,α毒素蛋白表达量为23.82%。动物实验结果表明,用重组菌株α毒素蛋白免疫的小鼠可以抵抗1MLD的A型产气荚膜梭菌标准株C57-1毒素攻击。     

Light scattering study of natural DNAs over a wide range of molecular weights: Evidence for compaction of the large molecules

This work reports light scattering measurements on DNA in aqueous solutions (100 mM NaCl, 1 mM EDTA and 10 mM Tris–HCl buffer, pH 7.8) over a wide range of molecular weights (10²–10⁵ base pairs) and shows that, in the above standard solvent, shorter chains (<10⁴ base pairs) behave as a “wormlike chain” and their diffusion coefficients as obtained by dynamic light scattering measurements, confirm the prediction of standard wormlike model, whilst longer chains (>10⁴ base pairs) behave in a different manner. Dynamic and static light scattering and SEM analysis indicate that DNA molecules 10⁵ base pairs long, condense into compact structures in our solvent conditions. Calculations done using a wormlike model are also presented and discussed in comparison both to our experimental data and to other data reported in the literature.     

Lack of Protective Osmolytes Limits Final Cell Density and Volumetric Productivity of Ethanologenic Escherichia coli KO11 during Xylose Fermentation

Limited cell growth and the resulting low volumetric productivity of ethanologenic Escherichia coli KO11 in mineral salts medium containing xylose have been attributed to inadequate partitioning of carbon skeletons into the synthesis of glutamate and other products derived from the citrate arm of the anaerobic tricarboxylic acid pathway. The results of nuclear magnetic resonance investigations of intracellular osmolytes under different growth conditions coupled with those of studies using genetically modified strains have confirmed and extended this hypothesis. During anaerobic growth in mineral salts medium containing 9% xylose (600 mM) and 1% corn steep liquor, proline was the only abundant osmolyte (71.9 nmol ml⁻¹ optical density at 550 nm [OD₅₅₀] unit⁻¹), and growth was limited. Under aerobic conditions in the same medium, twice the cell mass was produced, and cells contained a mixture of osmolytes: glutamate (17.0 nmol ml⁻¹ OD₅₅₀ unit⁻¹), trehalose (9.9 nmol ml⁻¹ OD₅₅₀ unit⁻¹), and betaine (19.8 nmol ml⁻¹ OD₅₅₀ unit⁻¹). Two independent genetic modifications of E. coli KO11 (functional expression of Bacillus subtilis citZ encoding NADH-insensitive citrate synthase; deletion of ackA encoding acetate kinase) and the addition of a metabolite, such as glutamate (11 mM) or acetate (24 mM), as a supplement each increased the intracellular glutamate pool during fermentation, doubled cell growth, and increased volumetric productivity. This apparent requirement for a larger glutamate pool for increased growth and volumetric productivity was completely eliminated by the addition of a protective osmolyte (2 mM betaine or 0.25 mM dimethylsulfoniopropionate), consistent with adaptation to osmotic stress rather than relief of a specific biosynthetic requirement.     

Growth phase-dependant enzyme profile of pyruvate catabolism and end-product formation in Clostridium thermocellum ATCC 27405

End-product synthesis and enzyme activities involved in pyruvate catabolism, H₂ synthesis, and ethanol production in mid-log (OD₆₀₀  0.25), early stationary (OD₆₀₀  0.5), and stationary phase (OD₆₀₀  0.7) cell extracts were determined in Clostridium thermocellum ATCC 27405 grown in batch cultures on cellobiose. Carbon dioxide, hydrogen, ethanol, acetate and formate were major end-products and their production paralleled growth and cellobiose consumption. Lactate dehydrogenase, pyruvate:formate lyase, pyruvate:ferredoxin oxidoreductase, methyl viologen-dependant hydrogenase, ferredoxin-dependant hydrogenase, NADH-dependant hydrogenase, NADPH-dependant hydrogenase, NADH-dependant acetaldehyde dehydrogenase, NADH-dependant alcohol dehydogenase, and NADPH-dependant alcohol dehydrogenase activities were detected in all extracts, while pyruate dehydrogenase and formate dehydrogenase activities were not detected. All hydrogenase activities decreased (2–12-fold) as growth progressed from early exponential to stationary phase. Alcohol dehydrogenase activities fluctuated only marginally (<45%), while lactate dehydrogenase, pyruvate:formate lyase, and pyruvate:ferredoxin oxidoreductase remained constant in all cell extracts. We have proposed a pathway involved in pyruvate catabolism and end-product formation based on enzyme activity profiles in conjunction with bioinformatics analysis.     

Purification of truncated and mutated Chemotaxis Inhibitory Protein of Staphylococcus aureus--an anti-inflammatory protein

The Chemotaxis Inhibitory Protein of Staphylococcus aureus (CHIPS) binds and blocks the C5a receptor (C5aR) and formyl-peptide receptor (FPR). This way, CHIPS is a potent inhibitor of the immune cell recruitment associated with inflammation. Truncation of the protein and the introduction of mutations, shifts the expression towards the insoluble fraction of Escherichia coli, whereas the wild-type protein can be solubly expressed. A protocol for expression and tag independent purification of biologically active CHIPS variants has been established to enable further characterization of an improved CHIPS variant, called ADC-1004. The CHIPS variants were purified by washing of E. coli inclusion bodies followed by refolding and gel filtration. New techniques were utilized to optimize the purification process. Expression in inclusion bodies was increased by the use of Ultra Yield^™ flasks and optimal refolding conditions were determined by the use of the iFOLD Refolding System 2^™.The folding and biological activity of the purified proteins were analyzed by circular dichroism (CD) spectroscopy and flow cytometry, respectively, and compared to solubly produced CHIPS_31–113 and wild-type CHIPS_1–121. We show that the CHIPS variants produced in inclusion bodies can be refolded and purified to achieve equal biological activity as solubly produced CHIPS_31–113 and wild-type CHIPS_1–121. The truncation causes minor structural changes while purification from inclusion bodies or the soluble fraction does not further affect the structure.     

Production of recombinant mink growth hormone in <Emphasis Type="Italic">E. coli</Emphasis>

Escherichia coli cells expressing mink (Mustela vison) growth hormone were grown in a batch fermentation process. The expression level was estimated to be 27% of the total cellular protein after 3 h of induction with 1 mM isopropyl β-d-thiogalactoside (IPTG). If the expression of mink growth hormone (mGH) was induced with 0.2 mM IPTG, the concentration of target protein was slightly lower and was found to be 23% at the same time after induction. mGH expressed as inclusion bodies was solubilized in 8 M urea and renatured by dilution protocol at a protein concentration of 1.4–2.1 mg/ml in the presence of glutathione pair in a final concentration of 11.3 mM. [GSH]/[GSSG] ratio equal to 2/1 was used. Two-step purification process comprising of ion-exchange chromatography on Q-Sepharose and hydrophobic chromatography on Phenyl-Sepharose was developed. Some 25–30 mg of highly purified and biologically active mGH was obtained from 4 g of biomass. The method presented in this study allows producing large quantities of mGH and considering initiation of scientific investigation on mGH effect on mink in vivo and availability in fur industry.     

High throughput purification of recombinant human growth hormone using radial flow chromatography

Recombinant human growth hormone (r-hGH) was expressed in Escherichia coli as inclusion bodies. Using fed-batch fermentation process, around 670 mg/L of r-hGH was produced at a cell OD600 of 35. Cell lysis followed by detergent washing resulted in semi-purified inclusion bodies with more than 80% purity. Purified inclusion bodies were homogenous in preparation having an average size of 0.6 μm. Inclusion bodies were solubilized at pH 12 in presence of 2 M urea and refolded by pulsatile dilution. Refolded protein was purified with DEAE-anion exchange chromatography using both radial and axial flow column (50 ml bed volume each). Higher buffer flow rate (30 ml/min) in radial flow column helped in reducing the batch processing time for purification of refolded r-hGH. Radial column based purification resulted in high throughput recovery of diluted refolded r-hGH in comparison to axial column. More than 40% of inclusion body protein could be refolded into bioactive form using the above method in a single batch. Purified r-hGH was analyzed by mass spectroscopy and found to be bioactive by Nb2 cell line proliferation assay. Inclusion body enrichment, mild solubilization, pulsatile refolding and radial flow chromatography worked co-operatively to improve the overall recovery of bioactive protein from inclusion bodies.     

Lactose Induction Increases Production of Recombinant Keratinocyte Growth Factor-2 in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Recombinant human keratinocyte growth factor-2 (rhKGF-2) has previously been expressed in Escherichia coli using isopropyl-β-d-thiogalactopyranoside (IPTG), a non-metabolizable and expensive compound, as the inducer. In order to determine whether IPTG could be replaced with the cheap and natural lactose to induce rhKGF-2 expression, we examined the expression of rhKGF-2 in flask culture and 30-l fermentation using lactose as the inducer. The optimized fermentation induced with lactose resulted in 1,382 g of cell mass, corresponding to a 84% enhancement in cell mass compared with IPTG induction. While the expression level of rhKGF-2 induced with lactose was comparable to that induced with IPTG, the solubility of target protein was increased by lactose induction than by IPTG induction. The recombinant protein was further purified by cation exchange and heparin-affinity chromatography. 255 milligrams of pure rhKGF-2 was achieved per liter culture by lactose induction, 52% higher than that obtained by IPTG induction. A preliminary biochemical characterization of purified rhKGF-2 was performed by Western blotting and mitogenic activity analysis, and the results demonstrated that the purified lactose-induced rhKGF-2 could react with anti-human KGF-2 antibody and stimulate the proliferation of FGFR2-IIIb-transfected mouse BaF3 cells as IPTG-induced rhKGF-2 could do.     

Production of steviol from steviol glucosides using β-glycosidase from Sulfolobus solfataricus

Steviol is a diterpene isolated from the plant Stevia rebaudiana that has a potential role as an antihyperglycemic agent by stimulating insulin secretion from pancreatic beta cells and also has significant potential to diminish the renal clearance of anionic drugs and their metabolites. In this study, the lacS gene, which encodes a thermostable β-glycosidase (SSbgly) enzyme from the extremely thermoacidophillic archaeon Sulfolobus solfataricus, was cloned and expressed in E. coli Rossetta BL21(DE3)pLyS using lactose as an inducer. Through fermentation, SSbgly was expressed as a 61 kDa protein with activity of 24.3 U/mg and the OD₆₀₀ of 23 was reached after 18 h induction with 10 mM lactose. Purified protein was obtained by Ni-Sepharose chromatography with a yield of 92.3%. SSbgly hydrolyzed steviol glycosides to produce steviol with a yield of 99.2%. The optimum conditions for steviol production were 50 U/ml SSbgly and 90 mg/ml Ste at 75 °C as determined by the response surface method.     

Localization and characterization of inclusion bodies in recombinant Escherichia coli cells overproducing penicillin G acylase

Various concentrations of isopropyl β-d-thiogalactopyranoside (IPTG) were used to induce production of the enzyme penicillin G acylase by recom binant Escherichia coli harboring plasmid pQEA11. The plasmid pQEA11 carries a wild-type pga gene, which is under the control of the tac promoter and lacI ^q. At low IPTG concentrations (0.025 – 0.1 mM), enzyme activity increased with increasing IPTG concentrations. At higher IPTG concentrations (0.2 and 0.5 mM), enzyme activity declined progressively. Examination of induced recombinant E. coli cells by transmission electron microscopy showed the presence of only periplasmic inclusion bodies at low IPTG concentrations (up to 0.1 mM) and both periplasmic and cytoplasmic inclusion bodies at high IPTG concentrations (0.2 mM and 0.5 mM). Results from sodium dodecyl sulfate/polyacrylamide gel electrophoresis and immunoblots of whole-cell proteins, membrane proteins and inclusion body proteins in these cells indicated that cytoplasmic inclusion bodies constituted an accumulation of preproenzyme (i.e., precursor polypeptide containing a signal peptide) and that periplasmic inclusion bodies constituted an accumulation of proenzyme (i.e., precursor polypeptide lacking a signal peptide). Received: 27 March 1996 / Received revision: 2 July 1996 / Accepted: 10 November 1996