High-level secretory production of human granulocyte-colony stimulating factor by fed-batch culture of recombinant Escherichia coli

Secretory production of human granulocyte colony-stimulating factor fusion protein (hG-CSF) by fed-batch culture of Escherichia coli was investigated in both 2.5-L and 30-L fermentors. To develop a fed-batch culture condition that allows efficient production of hG-CSF, different feeding strategies including pH-stat, exponential and constant feeding were examined. Among these, the constant feeding strategy (0.228 g glucose2min^-1) and the exponential feeding that supports a low specific growth rate (µ=0.116 h^-1) resulted in the best hG-CSF production. Under these conditions, 4.4 g2L^-1 of hG-CSF was produced. The effect of induction time on the protein production was also investigated. For the fed-batch cultures carried out with the pH-stat and exponential feeding strategies, induction at higher cell density (late-exponential phase) resulted in more hG-CSF production compared with induction at lower cell density (early to mid-exponential phase). The constant feeding strategy that supported best hG-CSF production was applied to the scale-up production of hG-CSF in 30 L of fermentor. The maximum dry cell weight and hG-CSF concentration of 51.7 and 4.2 g2L^-1, respectively, was obtained.     

Effects of carbon sources and feeding strategies on heparosan production by Escherichia coli K5

This work aimed to develop an optimal carbon source feeding strategy to achieve maximal production of heparosan as a precursor of bioengineered heparin by Escherichia coli K5. Glycerol gave higher heparosan titer and productivity compared to glucose. The maximum heparosan production (187 mg/L) and heparosan productivity (5.19 mg/L/h) in glycerol-defined medium were 26.4% higher than the heparosan production (148 mg/L) and heparosan productivity (4.11 mg/L/h) in glucose-defined medium. DO-stat feeding approach as compared to pH-stat feeding, exponential feeding, exponential combined with pH-stat feeding, and constant rate feeding gave the highest heparosan titer at 8.63 g/L, which was nine times that of batch culture. The obtained optimal glycerol feeding strategy may be useful for the scaling-up of microbial heparosan production.     

Excretion of human beta-endorphin into culture medium by using outer membrane protein F as a fusion partner in recombinant Escherichia coli

Escherichia coli BL21 strains were found to excrete a large amount of outer membrane protein F (OmpF) into culture medium during high-cell-density cultivation. From this interesting phenomenon, a novel and efficient OmpF fusion system was developed for the excretion of recombinant proteins by E. coli. The ompF gene of E. coli BL21(DE3) was first knocked out by using the red operon of bacteriophage lambda to construct E. coli MBEL-BL101. For the excretion of human beta-endorphin as a model protein, the beta-endorphin gene was fused to the C terminus of the E. coli ompF gene by using a linker containing the Factor Xa recognition site. To develop a fed-batch culture condition that allows efficient production of OmpF-beta-endorphin fusion protein, three different feeding strategies, an exponential feeding strategy and two pH-stat strategies with defined and complex nutrient feeding solutions, were examined. Among these, the pH-stat feeding strategy with the complex nutrient feeding solution resulted in the highest productivity (0.33 g of protein per liter per h). Under this condition, up to 5.6 g of OmpF-beta-endorphin fusion protein per liter was excreted into culture medium. The fusion protein was purified by anion-exchange chromatography and cleaved by Factor Xa to yield beta-endorphin, which was finally purified by reverse-phase chromatography. From 2.7 liters of culture supernatant, 545.4 mg of beta-endorphin was obtained.     

Comparative study of L-phenylalanine production in the growing and stationary phases during high cell density cultivation of an auxotrophic <Emphasis Type="Italic">Escherichia coli</Emphasis>

High cell density cultivation was investigated for L-phenylalanine (L-Phe) production by an L-tyrosine (L-Tyr) auxotrophic Escherichia coli WSH-BR165 (pAPB03). Dual exponential feeding of L-Tyr and glucose was adopted to achieve high cell density cultivation. The control was completed without dual feeding. The processes where dual feeding and induction were commenced together and those where induction began after dual feeding were studied and compared. The results indicated that the former dual feeding mode was most favorable for enhanced L-Phe production. With an optimal specific growth rate of 0.09/h during the dual exponential feeding period, the maximum dry cell weight reached 43.16 g/L (3.04 times that of the control) with a final L-Phe titer of 44.53 g/L (1.06 times that of the control) and an L-Phe productivity of 1.484 g/L/h (1.69 times that of the control). High cell density cultivation via the feeding of L-Tyr and glucose exponentially after the induction point proved to be an efficient approach to enhance L-Phe production.     

Production of heterologous thermostable glycoside hydrolases and the presence of host-cell proteases in substrate limited fed-batch cultures of Escherichia coli BL21(DE3)

Metabolic stress is a phenomenon often discussed in conjunction with recombinant protein production in Escherichia coli. This investigation shows how heterologous protein production and the presence of host cell proteases is related to: (1) Isopropyl-beta- D-thiogalactopyranoside (IPTG) induction, (2) cell-mass concentration at the time of induction, and (3) the presence of metabolites (glutamic acid or those from tryptone soy broth) during the post-induction phase of high cell density fed-batch cultivations. Two thermostable xylanase variants and one thermostable cellulase, all originating from Rhodothermus marinus, were expressed in E. coli strain BL21 (DE3). A three-fold difference in the specific activity of both xylanase variants [between 7,000 and 21,000 U/(g cell dry weight)], was observed under the different conditions tested. Upon induction at high cell-mass concentrations employing a nutrient feed devoid of the metabolites above, the specific activity of the xylanase variants, was initially higher but decreased 2-3 h into the post-induction phase and simultaneously protease activity was detected. Furthermore, protease activity was detected in all induced cultivations employing this nutrient feed, but was undetected in uninduced control cultivations (final cell-mass concentration of 40 g/l(-1)), as well as in induced cultivations employing metabolite-supplemented nutrient feeds. By contrast, maximum specific cellulase activity [between 700 and 900 U/(g cell dry weight)] remained relatively unaffected in all cases. The results demonstrate that detectable host cell proteases was not the primary reason for the decrease in post-induction activity observed under certain conditions, and possible causes for the differing production levels of heterologous proteins are discussed.     

From laboratory to pilot plant E. coli fed-batch cultures: optimizing the cellular environment for protein maximization

For recombinant protein production in E. coli fed-batch cultures, post-induction conditions have great influence in the quantity and quality of the product. The present paper covers the effect of different factors affecting the cellular environment in recombinant aldolase (rhamnulose-1-phosphate aldolase, RhuA) production. An operational mode employing an exponential addition profile for constant specific growth rate has been analyzed, in order to understand and define possible modifications with influence on post-induction cellular behavior. A constant addition profile has been demonstrated to render higher specific aldolase production than the exponential addition profile, probably due to a more constant environment for the cells. On the other hand, amino acid (leucine) supplementation has proven to increase protein quality in terms of activity units (U) per unit mass of RhuA (U mg^?1 RhuA), alleviating metabolic overload. Based on the above, a production process was set up and scaled up to pilot plant. Resulting production was double that of a standard laboratory operation, 45,000 U L^?1, and almost all the protein retained the 6xHis-tag with the highest quality, 11.3 U mg^?1 RhuA.     

Optimization of glucose feeding approaches for enhanced glucosamine and N-acetylglucosamine production by an engineered Escherichia coli

In this work, a recombinant Escherichia coli was constructed by overexpressing glucosamine (GlcN) synthase and GlcN-6-P N-acetyltransferase for highly efficient production of GlcN and N-acetylglucosamine (GlcNAc). For further enhancement of GlcN and GlcNAc production, the effects of different glucose feeding strategies including constant-rate feeding, interval feeding, and exponential feeding on GlcN and GlcNAc production were investigated. The results indicated that exponential feeding resulted in relatively high cell growth rate and low acetate formation rate, while constant feeding contributed to the highest specific GlcN and GlcNAc production rate. Based on this, a multistage glucose supply approach was proposed to enhance GlcN and GlcNAc production. In the first stage (0–2 h), batch culture with initial glucose concentration of 27 g/l was conducted, whereas the second culture stage (2–10 h) was performed with exponential feeding at μ _set = 0.20 h⁻¹, followed by feeding concentrated glucose (300 g/l) at constant rate of 32 ml/h in the third stage (10–16 h). With this time-variant glucose feeding strategy, the total GlcN and GlcNAc yield reached 69.66 g/l, which was enhanced by 1.59-fold in comparison with that of batch culture with the same total glucose concentration. The time-dependent glucose feeding approach developed here may be useful for production of other fine chemicals by recombinant E. coli.     

补加前体L-蛋氨酸对高密度发酵生产S-腺苷-L-蛋氨酸的影响

将高密度发酵技术成功应用于S-腺苷-L-蛋氨酸的生产。考察了补加前体L-蛋氨酸的量以及补加策略对酿酒酵母G14发酵生产S-腺苷-L-蛋氨酸的影响。实验发现补加前体L-蛋氨酸能明显促进S-腺苷-L-蛋氨酸的积累。同时还发现不同的补加策略对菌体浓度以及S-腺苷-L-蛋氨酸的产量和浓度有不同的影响。确定了补加L-蛋氨酸不应低于0.7g/10g菌体干重。比较了五种不同的补加前体L-蛋氨酸的方式。结果表明在菌体干重达到高密度的情况下(120g/L)补加前体L-蛋氨酸进行转化生产S-腺苷-L-蛋氨酸能达到比较好的效果一次性补加9g L-蛋氨酸,SAM的积累量在补加后的18h达到最高,为4.31g/L;采取流加方式补加L-蛋氨酸,流加速率为2g/h,共流加5h,流加结束28h后SAM达到最高积累量后者达到4.98g/L。两者最终的生物量均可达到130g/L以上。     

Fed-batch culture of recombinant NS0 myeloma cells with high monoclonal antibody production

An amplified NS0 cell line transfected with a vector expressing a humanized monoclonal antibody (MAb) against CD-18 and glutamine synthetase (GS) was cultivated in a 1.5 L fed-batch culture using a serum-free, glutamine-free medium. Concentrated solutions of key nutrient components were fed periodically using a simple feeding control strategy. Feeding amounts were adjusted daily based on the integral of viable cell concentration over time (IVC) and assumed constant specific nutrient consumption rates or yields to maintain concentrations of the key nutrient components around their initial levels. On-line oxygen uptake rate (OUR) measurement was used to aid empirically the adjustment of the feeding time points and amounts by inferring time points of nutrient depletion. Through effective nutritional control, both cell growth phase and culture lifetime were prolonged significantly, resulting in a maximal viable cell concentration of 6.6 x 10(9) cells/L and a final IVC of 1.6 x 10(12) cells-h/L at 672 h. The final MAb concentration reached more than 2.7 g/L. In this fed-batch culture, cellular metabolism shifts were repeatedly observed. Accompanying the culture phase transition from the exponential growth to the stationary phase, lactate, which was produced in the exponential growth phase, became consumed. The time point at which this metabolism shift occurred corresponded to that of rapid decrease of OUR, which most likely was caused by nutrient depletion. This transition coincided with the onset of ammonia, glutamate and glutamine accumulation. With removal of the nutrient depletion by increasing the daily nutrient feeding amount, OUR recovered and viable cell concentration increased, while cell metabolism shifted again. Instead of consumption, lactate became produced again. These results suggest close relationships among nutrient depletion, cell metabolism transition, and cell death. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 783-792, 1997.     

Excretion of Human β-Endorphin into Culture Medium by Using Outer Membrane Protein F as a Fusion Partner in Recombinant Escherichia coli

Escherichia coli BL21 strains were found to excrete a large amount of outer membrane protein F (OmpF) into culture medium during high-cell-density cultivation. From this interesting phenomenon, a novel and efficient OmpF fusion system was developed for the excretion of recombinant proteins by E. coli. The ompF gene of E. coli BL21(DE3) was first knocked out by using the red operon of bacteriophage λ to construct E. coli MBEL-BL101. For the excretion of human β-endorphin as a model protein, the β-endorphin gene was fused to the C terminus of the E. coli ompF gene by using a linker containing the Factor Xa recognition site. To develop a fed-batch culture condition that allows efficient production of OmpF-β-endorphin fusion protein, three different feeding strategies, an exponential feeding strategy and two pH-stat strategies with defined and complex nutrient feeding solutions, were examined. Among these, the pH-stat feeding strategy with the complex nutrient feeding solution resulted in the highest productivity (0.33 g of protein per liter per h). Under this condition, up to 5.6 g of OmpF-β-endorphin fusion protein per liter was excreted into culture medium. The fusion protein was purified by anion-exchange chromatography and cleaved by Factor Xa to yield β-endorphin, which was finally purified by reverse-phase chromatography. From 2.7 liters of culture supernatant, 545.4 mg of β-endorphin was obtained.     

Enhanced growth of Sf-9 cells to a maximum density of 5.2 x 10(7) cells per mL and production of beta-galactosidase at high cell density by fed batch culture

Significant improvement in cell growth and protein production has been achieved in Sf-9 insect cell cultures using pulse additions of multicomponent nutrient feed concentrates (Bédard et al., 1994; Chan et al., 1998). The present work focuses on investigating an alternative feeding strategy wherein the nutrients are fed in a semi continuous manner. Fed batch culture experiments were carried out to compare the two different feeding strategies, pulse and semi continuous and a process developed to achieve a cell density of 5.2 x 10(7) cells/mL of Sf-9 cells in a 3.5 L bioreactor. Production of recombinant protein beta-galactosidase was carried out by infecting the cells with baculovirus at a MOI of 10 at cell densities of 17 x 10(6)cells/mL. Specific productivity could be maintained at cell densities as high as 14 x 10(6) cells/mL. The results presented indicate that the feeding method can provide significant improvements in the performance with a reduction in the amount of total nutrients added. On-line monitoring of the culture using the capacitance probe showed that the capacitance probe can be used successfully to monitor the biomass and infection process even at higher cell densities.     

Optimization of fed-batch parameters and harvest time of CHO cell cultures for a glycosylated product with multiple mechanisms of inactivation

Optimization of fed-batch feeding parameters was explored for a system with multiple mechanisms of product inactivation. In particular, two separate mechanisms of inactivation were identified for the recombinant tissue-type activator (r-tPA) protein. Dynamic inactivation models were written to describe particular r-tPA glycoform inactivation in the presence and absence of free-glucose. A glucose-independent inactivation mechanism was identified, and inactivation rate constants were found dependent upon the presence of glycosylation of r-tPA at N184. Inactivation rate constants of the glucose-dependent mechanism were not affected by glycosylation at N184. Fed-batch optimization was performed for r-tPA production by CHO cell culture in a stirred-tank reactor with glucose, glutamine and asparagine feed. Feeding profiles in which culture supernatant concentrations of free-glucose and amino acids (combined glutamine and asparagine) were used as control variables, were evaluated for a wide variety of set points. Simulation results for a controlled feeding strategy yielded an optimum at set points of 1.51 g L(-1) glucose and 1.18 g L(-1) of amino acids. Optimization was also performed in absence of metabolite control using fixed feed-flow rates initiate during the exponential growth phase. Fixed feed-flow results displayed a family of optimum solutions along a mass flow rate ratio of 3.15 of glucose to amino acids. Comparison of the two feeding strategies showed a slight advantage of rapid feeding at a fixed flow rate as opposed to metabolite control for a product with multiple mechanisms of inactivation.     

Feeding strategies for the enhanced production of α-arbutin in the fed-batch fermentation of Xanthomonas maltophilia BT-112

To develop a cost-effective method for the enhanced production of α-arbutin using Xanthomonas maltophilia BT-112 as a biocatalyst, different fed-batch strategies such as constant feed rate fed-batch, constant hydroquinone (HQ) concentration fed-batch, exponential fed-batch and DO-control pulse fed-batch (DPFB) on α-arbutin production were investigated. The research results indicated that DPFB was an effective method for α-arbutin production. When fermentation with DO-control pulse feeding strategy to feed HQ and yeast extract was applied, the maximum concentrations of α-arbutin and cell dry weight were 61.7 and 4.21 g/L, respectively. The α-arbutin production was 394 % higher than that of the control (batch culture) and the molar conversion yield of α-arbutin reached 94.5 % based on the amount of HQ supplied (240 mM). Therefore, the results in this work provide an efficient and easily controlled method for industrial-scale production of α-arbutin.     

Fed-batch sorbose fermentation using pulse and multiple feeding strategies for productivity improvement

Microbial oxidation of D-sorbitol tol-sorbose byAcetobacter suboxydans is of commercial importance since it is the only biochemical process in vitamin C synthesis. The main bottleneck in the batch oxidation of sorbitol to sorbose is that the process is severely inhibited by sorbitol. Suitable fed-batch fermentation designs can eliminate the inherent substrate inhibition and improve sorbose productivity. Fed-batch sorbose fermentations were conducted by using two nutrient feeding strategies. For fed-batch fermentation with pulse feeding highly concentrated sorbitol (600 g/L) along with other nutrients were fed intermittently in four pulses of 0.5 liter in response to the increased DO signal. The fed-batch fermentation was over in 24 h with a sorbose productivity of 13.40 g/L/h and a final sorbose concentration of 320.48 g/L. On the other hand, in fed-batch fermentation with multiple feeds, two pulse feeds of 0.5 liter nutrient medium containing 600 g/L sorbitol was followed by the addition of 1.5 liter nutrient medium containing 600 g/L sorbitol at a constant feed rate of 0.36 L/h till the full working capacity of the reactor. The fermentation was completed in 24 h with an enhanced sorbose productivity of 15.09 g/L/h and a sorbose concentration of 332.60 g/L. The sorbose concentration and productivity obtained by multiple feeding of nutrients was found to be higher than that obtained by pulse feeding and was therefore a better strategy for fed-batch sorbose fermentation.     

A rational approach to improving productivity in recombinant Pichia pastoris fermentation

A Mut(S) Pichia pastoris strain that had been genetically modified to produce and secrete sea raven antifreeze protein was used as a model system to demonstrate the implementation of a rational, model-based approach to improve process productivity. A set of glycerol/methanol mixed-feed continuous stirred-tank reactor (CSTR) experiments was performed at the 5-L scale to characterize the relationship between the specific growth rate and the cell yield on methanol, the specific methanol consumption rate, the specific recombinant protein formation rate, and the productivity based on secreted protein levels. The range of dilution rates studied was 0. 01 to 0.10 h(-1), and the residual methanol concentration was kept constant at approximately 2 g/L (below the inhibitory level). With the assumption that the cell yield on glycerol was constant, the cell yield on methanol increased from approximately 0.5 to 1.5 over the range studied. A maximum specific methanol consumption rate of 20 mg/g. h was achieved at a dilution rate of 0.06 h(-1). The specific product formation rate and the volumetric productivity based on product continued to increase over the range of dilution rates studied, and the maximum values were 0.06 mg/g. h and 1.7 mg/L. h, respectively. Therefore, no evidence of repression by glycerol was observed over this range, and operating at the highest dilution rate studied maximized productivity. Fed-batch mass balance equations, based on Monod-type kinetics and parameters derived from data collected during the CSTR work, were then used to predict cell growth and recombinant protein production and to develop an exponential feeding strategy using two carbon sources. Two exponential fed-batch fermentations were conducted according to the predicted feeding strategy at specific growth rates of 0.03 h(-1) and 0.07 h(-1) to verify the accuracy of the model. Cell growth was accurately predicted in both fed-batch runs; however, the model underestimated recombinant product concentration. The overall volumetric productivity of both runs was approximately 2.2 mg/L. h, representing a tenfold increase in the productivity compared with a heuristic feeding strategy.     

补料方式对酵母菌生产谷胱甘肽的影响

比较了酵母菌发酵生产谷胱甘肽（GSH）的几种补料分批培养方式。实验发现补料可以明显地促进酵母菌的生长和谷胱甘肽的合成,同时还发现不同的补料方式对发酵液中的菌体浓度和GSH浓度有不同的影响。采用指数流加方式可获得极高的菌体浓度,但菌体中的GSH浓度较低;而采用恒－pH补料分批培养既可以达到较高菌体浓度,菌体中又含有较高的GSH含量,因此,其总的GSH产量最高,可达到977.8mg/L。     

基于动力学模型的法夫酵母发酵生产虾青素的补料策略优化

对法夫酵母的不同补料发酵方式进行了研究.基于底物抑制模型,提出了一种优化的两阶段补料策略,用于法夫酵母产虾青素的高密度发酵.在发酵的延迟期和对数生长期早期,糖浓度控制在25 g/L左右,在此条件下,生物量可以达到最大,且时间缩短.在对数生长期后期及稳定期,糖浓度控制在5 g/L,虾青素的合成时间可以有效延长.与传统的补料方式相比,采用此补料策略取得了较好的发酵效果.发酵终点细胞干重达到23.8g/L,虾青素产量达到29.05 mg/L,分别比分批发酵提高了52.8%和109%.     

Effect of methanol feeding strategies on production and yield of recombinant mouse endostatin from Pichia pastoris

Pichia pastoris, a methylotrophic yeast, is an efficient producer of recombinant proteins in which the heterologous gene is under the control of the methanol-induced AOX1 promoter. Hence, the accepted production procedure has two phases: In the first phase, the yeast utilizes glycerol and biomass is accumulated; in the second phase, the yeast utilizes methanol which is used both as an inducer for the expression of the recombinant protein and as a carbon source. Since the yeast is sensitive to methanol concentration, the methanol is supplied gradually to the growing culture. Three methanol addition strategies were evaluated for the purpose of optimizing recombinant endostatin production. Two strategies were based on the yeast metabolism; one responding to the methanol consumption using a methanol sensor, and the other responding to the oxygen consumption. In these two strategies, the methanol supply is unlimited. The third strategy was based on a predetermined exponential feeding rate, controling the growth rate at 0.02 h(-1), in this strategy the methanol supply is limited. Throughout the induction phase glycerol, in addition to methanol, was continuously added at a rate of 1 g L h(-1). Total endostatin production was similar in all three strategies, (400 mg was obtained from 3 L initial volume), but the amount of methanol added and the biomass produced were lower in the predetermined rate method. This caused the specific production of endostatin per biomass and per methanol to be 2 times higher in the predetermined rate than in the other two methods, making the growth control strategy not only more efficient but also more convenient for downstream processing.     

Optimization of a cultivation process for recombinant protein production by Escherichia coli.

A single-stage fed-batch bioprocess for the production of a recombinant protein beta-galactosidase, by E. coli has been developed. The XL1-blue strain of E. coli which harbors a multi-number foreign plasmid PT was cultured in a reformulated medium. Critical medium components were selected and their respective concentrations were optimized with the Orthogonal Table method. An exponential substrate feeding schedule was used to maintain optimum conditions. Inhibition of growth and protein expression caused by excessive concentrations of glucose and acetate was investigated and subsequently minimized with an incremental nutrient feeding schedule which limited the specific growth rate of a culture. The program necessary to facilitate the control of substrate addition is fully described. This program has been used with a 2.5 l bioreactor and a commercially available software package for optimization without on-line or off-line measurement of optical density (OD), CO2, glucose or acetate. The optimized fed-batch process limited the acetate concentration to less than 20 mM; maintained an exponential growth phase for 50 h; and produced a cell density of 51 g l-1 dry cell weight (DCW) or 154 OD600 with a beta-galactosidase activity of 990 U ml-1.     

Effects of post-induction feed strategies on secretory production of recombinant streptokinase in Escherichia coli

The effects of post-induction nutrient feed rates, on recombinant streptokinase production in fed-batch processes, were investigated using various feed profiles. Recombinant streptokinase was produced using a secretory expression system and was induced by a temperature up-shift, using a temperature-sensitive λ_PL promoter. The specific growth rates decreased sharply upon induction of recombinant protein expression, thus necessitating a variable feed strategy in the post-induction phase. The various feed profiles employed in the post-induction phase included constant feed rates, linearly increasing feed rate and exponentially varying feed rates. Significant differences were obtained in the specific activity of streptokinase produced in these fed-batch processes. A maximum activity per unit biomass of 4.96 × 10⁶ and 4.43 × 10⁶ IU/g DCW was achieved for exponentially decreasing feed and linearly increasing feed, respectively. The decrease in specific growth rate during the post-induction phase was also less pronounced in these cases in comparison to other fed-batch experiments. It was observed that streptokinase productivity is governed by the nutrient feed rate per unit biomass at a critical juncture after induction. The highest activity per unit biomass was obtained when the nutrient feed rate per unit biomass was around 0.7–0.8 g glucose (g DCW)⁻¹ h⁻¹, between 2 and 4 h after induction.