Cyclic fed-batch culture for production of human serum albumin in Pichia pastoris

Simple cyclic fed-batch culture (cfbc), consisting of a constant medium feed with periodic withdrawals of culture, resulted in a product yield (13.4 mg protein per gram biomass) similar to that obtained using the complex multiphase industrial production strategy (13.7 mg protein per gram biomass). In cfbc, productivity was ultimately limited by the rate at which the cells could assimilate methanol. Glycerol was inhibitory to growth at high concentrations. However, product yield continued to increase as the glycerol concentration was increased. In chemostat culture, dissolved oxygen concentration influenced product yield independently of any detectable influence on cell growth.     

Optimization of human serum albumin production in methylotrophic yeast Pichia pastoris by repeated fed-batch fermentation

An optimization method for repeated fed-batch fermentation was established with the aim of improving the recombinant human serum albumin (rHSA) production in Pichia pastoris. A simulation model for fed-batch fermentation was formulated and the optimal methanol-feeding policy calculated by dynamic programming method using five different methanol-feeding periods. The necessary state variables were collected from the calculated results and used for further optimization of repeated fed-batch fermentation. The optimal operation policy was investigated using the pre-collected state variables by estimating the overall profit per total methanol-feeding time. The calculated results indicated that the initial cell mass from the 2nd fed-batch fermentation on should be set at 35 or 40 g and methanol-feeding time at 264 h. In repeated fed-batch fermentation using the optimal operation policy, actual culture volume was in good agreement with the values simulated by model equations, but some discrepancy was observed in rHSA production. Minimum experiments were therefore carried out to re-evaluate rHSA production levels, which were then applied in re-calculations to determine the optimal operation policy. The optimal policy for repeated fed-batch fermentation established in the present study (i.e., 4-times-repeated fed-batch fermentation) achieved a 47% increase in annual rHSA production. Optimization of the culture period also brought about a 28% increase in annual rHSA production even in simple (not repeated) fed-batch fermentation.     

Optimization of the production of a honeybee odorant-binding protein by Pichia pastoris

A honeybee putative general odorant-binding protein ASP2 has been expressed in the methylotrophic yeast Pichia pastoris. It was secreted into the buffered minimal medium using either the alpha-factor preprosequence with and without the Glu-Ala-Glu-Ala spacer peptide of Saccharomyces cerevisiae or its native signal peptide. Whereas ASP2 secreted using the alpha-factor preprosequence with the spacer peptide showed N-terminal heterogeneity, the recombinant protein using the two other secretion peptides was correctly processed. Mass spectrometry showed that the protein secreted using the natural peptide sequence had a mass of 13,695.1 Da, in perfect agreement with the measured molecular mass of the native protein. These data showed a native-like processing and the three disulfide bridges formation confirmed by sulfhydryl titration analysis. After dialysis, the recombinant protein was purified by one-step anion-exchange chromatography in a highly pure form. The final expression yield after 7-day fermentation was approximately 150 mg/liter. To our knowledge, this is the first report of the use of a natural insect leader sequence for secretion with correct processing in P. pastoris. The overproduction of recombinant ASP2 should allow ligand binding and mutational analysis to understand the relationships between structure and biological function of the protein.     

A novel feeding strategy for enhanced protein production by fed-batch fermentation in recombinant Pichia pastoris

A novel feeding strategy for enhanced protein production of hepatitis B virus surface antigen (HBsAg) in fed-batch fermentation, recombinant Pichia pastoris, has been developed. A minimal salt medium was used to grow cells in the initial batch fermentation, followed by a glycerol+salts fed-batch phase. At the end of the fed-batch phase a dry cell weight of 130 g l⁻¹ was achieved. In the absence of basal salts, the same amount of glycerol feed resulted in only 90 g l⁻¹ cell dry weight. When a limited amount of casamino acids were also included every 24 h during methanol induction, there was a two-fold increase in expression levels of HBsAg. After 192 h of induction, the expression levels of HBsAg (soluble and insoluble) reached >1 g l⁻¹ using the Mut⁻ strain. Thus, the use of basal salts in the glycerol feed, along with the addition of limited amounts of casamino acids with the methanol feed, resulted in an increased expression of total HBsAg.     

Enhancing the production of Fc fusion protein in fed-batch fermentation of Pichia pastoris by design of experiments

This study focuses on the feasibility of producing a therapeutic Fc fusion protein in Pichia pastoris (P. pastoris) and presents an optimization design of experiment (DOE) strategy in a well-defined experimental space. The parameters examined in this study include pH, temperature, salt supplementation, and batch glycerol concentration. The effects of these process conditions were captured by statistical analysis focusing on growth rate and titer responses. Batch medium and fermentation conditions were also investigated prior to the DOE study in order to provide a favorable condition to enable the production of this Fc fusion protein. The results showed that approximately 373 mg/L of the Fc fusion protein could be produced. The pH was found to be particularly critical for the production of this Fc fusion protein. It was significantly higher than the conventional, recommended pH for P. pastoris fermentation. The development of this process shows that protein production in P. pastoris is protein specific, and there is not a set of pre-defined conditions that can work well for all types of proteins. Thorough process development would need to be performed for every type of protein in order for large-scale production in P. pastoris to be feasible.     

重组毕赤酵母产植酸酶发酵条件的优化

为研究优化毕赤酵母工程菌H311产植酸酶的发酵条件,采用单因素试验和L18(37)正交试验考察不同工艺条件对产酶活性的影响。结果表明:影响重组毕赤酵母产植酸酶的因素重要性从大到小依次为诱导时间、甲醇添加量、装液量、初始诱导p H、生长时间、接种量和初始生长p H,产酶最佳条件为接种量3%(体积分数)、装液量20 m L(250 m L摇瓶)、生长时间20 h,诱导时间120 h、甲醇添加量1.5%(体积分数)、生长p H 6.0、诱导p H 5.0,在此条件下进行诱导表达,植酸酶的比酶活可达334 U/m L。     

发酵重组Pichia pastoris生产腺苷甲硫氨酸的研究

在5L发酵罐中对高产S腺苷甲硫氨酸的重组Pichia pastoris发酵进行了研究。重组菌在pH5．0生长,然后调为pH6．0积累腺苷甲硫氨酸,在30℃、溶氧5％及流加甲硫氨酸和尿素的条件下培养82h后,产量达4．3g／L。     

重组巴斯德毕赤酵母发酵生产内切几丁质酶的培养条件优化

探讨重组巴斯德毕赤酵母发酵生产内切几丁质酶的最适培养条件,以期获得最佳的内切几丁质酶活力。以内切几丁质酶活力为指标,通过部分因子试验设计以及响应面法优化确定重组巴斯德毕赤酵母高产内切几丁质酶的最适培养条件。部分因子试验设计筛选的影响重组巴斯德毕赤酵母高产内切几丁质酶的3个关键因子为甲醇、油酸和吐温-80。响应面法优化的上述3个关键因子的最佳浓度分别为0.71%、0.086%和0.31%。重组巴斯德毕赤酵母发酵生产内切几丁质酶的最适培养条件为：酵母膏1%、酵母氮碱（YNB）1.34%、蛋白胨2%、甲醇0.71%、油酸0.086%、吐温-80 0.31%、PTM₁ 0.8%、pH 6.0。在上述培养条件下,重组巴斯德毕赤酵母产内切几丁质酶的活力高达30.92U/mL。与未优化前相比,酶活力提高了1.44倍。研究结果为内切几丁质酶的产业化生产和应用奠定了良好基础。     

Oxygen-limited fed-batch process: an alternative control for Pichia pastoris recombinant protein processes

An oxygen-limited fed-batch technique (OLFB) was compared to traditional methanol-limited fed-batch technique (MLFB) for the production of recombinant Thai Rosewood β-glucosidase with Pichia pastoris. The degree of energy limitation, expressed as the relative rate of respiration (q _O/q _O,max), was kept similar in both the types of processes. Due to the higher driving force for oxygen transfer in the OLFB, the oxygen and methanol consumption rates were about 40% higher in the OLFB. The obligate aerobe P. pastoris responded to the severe oxygen limitation mainly by increased maintenance demand, measured as increased carbon dioxide production per methanol, but still somewhat higher cell density (5%) and higher product concentrations (16%) were obtained. The viability was similar, about 90–95%, in both process types, but the amount of total proteins released in the medium was much less in the OLFB processes resulting in substantially higher (64%) specific enzyme purity for input to the downstream processing.     

Two-stage glycerol feeding for enhancement of recombinant hG-CSF production in a fed-batch culture of Pichia pastoris

Recombinant hG-CSF was expressed in Pichia pastoris under the control of the AOX1 promoter. In this study, the glycerol feeding rate was adjusted to achieve the maximum attainable specific growth rate before induction. Using a two-stage glycerol feeding method, the specific growth rate was changed from a maximum value of 0.21 h⁻¹ (at the beginning of feeding) to 0.15 h⁻¹ prior to induction. With this approach, the final dry cell wt and rhG-CSF yield achieved was close to 120 g l⁻¹ and 320 mg l⁻¹, respectively. Our study found that the two-stage feeding method allowed the overall productivity of rhG-CSF to increase 2.9 times that of the conventional fed-batch method.     

Maximization of production of secreted recombinant proteins in Pichia pastoris fed-batch fermentation

Pontryagin's Maximum Principle has been applied for optimization of secreted proteins from Pichia pastoris fed-batch fermentation. The objective of this work is to maximize the total accumulated product per unit operation time under different given conditions and system constraints. To obtain optimal solutions, an automated curve-fitting software, Table Curve 2D, was employed to construct the necessary mathematical models and solve the complicated functions. In the solution processes, the end of the glycerol batch phase was defined as the initial state of the system, the end of the methanol fed-batch phase as the final state, the cell mass produced along with product accumulated as state variables, and the specific growth rate (mu) as the control variable. Initially, a relationship between the specific production rate (rho) and mu was established. Then, according to Pontryagin's Maximum Principle, the admissible range of mu and its trajectories for the optimal operations were determined. Four representative cases with different combinations of the operation time along with the initial and final states were evaluated. A close correlation was obtained between the predicted values of the model equation with the experimental results from the Pichia pastoris fed-batch fermentations producing secreted alpha-galactosidase. The approaches proposed here greatly simplify the computational processes and validate the optimization strategy as a generalized approach to maximize the yield from fed-batch fermentations.     

Optimization of the fermentation parameters for the production of Ganoderma lucidum immunomodulatory protein by Pichia pastoris

Abstract

In order to obtain a better fermentation parameter for the production of recombinant Ganoderma lucidum immunomodulatory protein (rFIP-glu), an engineered Pichia pastoris GS115 was investigated on the fermentation time, temperature, methanol concentration and initial pH of media, while immunomodulatory activities of the rFIP-glu was confirmed. L₉(3³) orthogonal experiment were firstly employed to optimize various fermentation parameters in the shake-flask level. The optimized fermentation parameters were subsequently verified in a 5?L fermenter. Biological activities including cell viability and tumor necrosis factor-alpha (TNF-α) mRNA of the rFIP-glu were evaluated on murine macrophage RAW264.7 cells. The results showed that the yield of rFIP-glu was up to 368.71?μg/ml in the shake-flask, and 613.47?μg/ml in the 5?L fermenter, when the Pichia pastoris was incubated in basic media with the methanol concentration 1.0% and initial pH 6.5, and with constant shaking at 280?rpm for 4?days at 26?°C. In vitro assays of biological activity indicated that rFIP-glu had significant toxicity against RAW264.7 cells, and possessed the ability to induce TNF-α mRNA expression in macrophage RAW264.7 cells. In conclusion, engineered P. pastoris showed a good fermentation property under the optimum fermentation parameters. It could be a candidate industrial strain for further study.     

Optimization of the wheat puroindoline-a production in Pichia pastoris

AIMS: A recombinant puroindoline-a (rPIN-a) was produced using the methylotrophic yeast Pichia pastoris. METHODS AND RESULTS: In fed-batch culture, the production of rPIN-a decreased after 24 h of methanol induction. Most of the rPIN-a was not soluble in the culture medium remaining bound to the cell walls. Soluble and membrane-bound rPIN-a were quantified by ELISA after Triton X-114 phase partitioning. In order to improve the production of rPIN-a, the influence of pH, specific growth rate and the addition of TX-114 was tested on two independent continuous cultures. The production of rPIN-a was improved when continuous culture was carried out at 29 degrees C under acid conditions (pH 5) with a low dilution rate (D=0.025 h(-1)). The addition of 0.01% TX-114 to the medium inverted the ratio between the secreted and the membrane-bound rPIN-a. CONCLUSION: When a continuous culture was carried out under optimized conditions, the rPIN-a production yield was increased 10-fold to 14 mg l(-1) and 80% of the rPIN-a was soluble. SIGNIFICANCE AND IMPACT OF THE STUDY: This study would be helpful to optimize the expression of other membrane-bound proteins in P. pastoris.     

重组毕赤酵母发酵生产S-腺苷甲硫氨酸培养条件优化

甲醇营养型毕赤酵母生产S-腺苷甲硫氨酸(SAM)是通过其表达的SAM合成酶催化L-甲硫氨酸(L-Met)和ATP反应而合成的。本文采用全合成培养基,在摇瓶上进行了培养条件的优化,确定了接种量、pH、PTM1、PO43-等初步条件。并根据SAM生物合成的特征,重点对其碳、氮源的影响作了进一步的分析优化。结果表明:当CaSO40.465g/L,K2SO49.10g/L,MgSO4.7H2O 7.45g/L,PO43-0.5mol/L情况下,生长阶段,甘油4%、硫酸铵4.00g/L为最佳;诱导表达阶段,L-Met1.0g/L,甘油与甲醇比例为0.5、硫酸铵8.00g/L为最佳。优化后,SAM产量诱导4d后达1.48g/L,诱导5d后可达1.70g/L(131mg/g干细胞),L-Met的转化率可达40.65%,既利于工艺放大又便于产品的分离纯化。     

Optimization of erythritol production by Candida magnoliae in fed-batch culture

A two-stage fed-batch process was designed to enhance erythritol productivity by the mutant strain of Candida magnoliae. The first stage (or growth stage) was performed in the fed-batch mode where the growth medium was fed when the pH of the culture broth dropped below 4.5. The second stage (or production stage) was started with addition of glucose powder into the culture broth when the cell mass reached about 75 g dry cell weight l⁻¹. When the initial glucose concentration was adjusted to 400 g l⁻¹ in the production stage, 2.8 g l⁻¹ h⁻¹ of overall erythritol productivity and 41% of erythritol conversion yield were achieved, which represented a fivefold increase in erythritol productivity compared with the simple batch fermentation process. A high glucose concentration in the production phase resulted in formation of organic acids including citrate and butyrate. An increase in dissolved oxygen level caused formation of gluconic acid instead of citric acid. Journal of Industrial Microbiology & Biotechnology (2000) 25, 100–103. Received 25 February 2000/ Accepted in revised form 08 June 2000     

Analysis and control of proteolysis of a fusion protein in Pichia pastoris fed-batch processes

A fusion protein composed of a cellulose-binding module (CBM) from Neocallimastix patriciarum cellulase 6A and lipase B from Candida antarctica (CALB), was produced by Pichia pastoris Mut(+) in high-cell density bioreactor cultures. The production was induced by switching from growth on glycerol to growth on methanol. The lipase activity in the culture supernatant increased at an almost constant rate up to a value corresponding to 1.3 g x l(-1) of CBM-CALB. However, only about 40% of the product was of full-length according to Western blot analysis. This loss was due to a cleavage of the protein in the linker between the CBM and the CALB moieties. The cleavage was catalyzed by serine proteases in the culture supernatant. The CALB-moiety was subjected to further slow degradation by cell-associated proteolysis. Different strategies were used to reduce the proteolysis. Previous efforts to shorten the linker region resulted in a stable protein but with ten times reduced product concentration in bioreactor cultures (Gustavsson et al. 2001, Protein Eng. 14, 711-715). Addition of rich medium for protease substrate competition had no effect on the proteolysis of CBM-CALB. The kinetics for the proteolytic reactions, with and without presence of cells were shown to be influenced by pH. The fastest reaction, cleavage in the linker, was substantially reduced at pH values below 5.0. Decreasing the pH from 5.0 to 4.0 in bioreactor cultures resulted in an increase of the fraction of full-length product from 40 to 90%. Further improvement was achieved by decreasing the temperature from 30 to 22 degrees C during the methanol feed phase. By combining the optimal pH and the low temperature almost all product (1.5 g x l(-1)) was obtained as full-length protein with a considerably higher purity in the culture supernatant compared with the original cultivation.     

Interest of fed-batch culture for the production of a membrane-bound protein by an adherent animal cell

The production of a membrane-bound protein by culture and harvesting of r-CHO cells has been evaluated. While in batch culture, the maximal cell density is only maintained for a few hours, in a fed-batch one, the cell and enzyme concentrations, as well as the growth and production rates, can be kept constant during 100 hours. This stabilized phase facilitates the cell harvesting and provides a kinetic tool for testing chemical molecules as sodium butyrate.     

重组毕赤酵母高密度发酵生产内切型纤维素酶的条件优化

为优化内切型纤维素酶高密度发酵工艺条件,在7.5L发酵罐高密度发酵条件下,研究内切型纤维素酶表达量以及毕赤酵母胞外蛋白酶合成水平的影响因素。研究表明:经340mL甘油补料发酵后,在甲醇诱导阶段,pH为5.0,温度为25℃,利用甲醇检测流加控制器控制甲醇体积分数为0.33%～0.35%时,EGI表达量可达421.1IU/mL,比采用固定甲醇流加速率的发酵方法提高了1.49倍。     

Optimization of the high-level production of Rhizopus oryzae lipase in Pichia pastoris

The lipases of the Rhizopus species family are important and versatile enzymes that are mainly used in fat and oil modification due to their strong 1,3-regiospecificity. Inexpensive synthetic medium was used for the production of Rhizopus oryzae lipase in the methylotrophic yeast Pichia pastoris. Methanol accumulation inside the bioreactor has previously been shown to negatively influence the production level. Three different methanol fed-batch strategies for maintaining the methanol concentration within optimal limits have been assayed in high-density cultures. One methanol feeding strategy, which is based on the monitoring of the methanol concentration by gas chromatography, resulted in a 2.5-fold higher productivity compared to an initial cultivation, where the feeding rate was adjusted according to the dissolved oxygen concentration (DO) in the supernatant. Finally, productivity could be further increased by introducing a transition phase that involved the simultaneous feeding of glycerol and methanol followed by a single methanol feed. This optimized strategy resulted in the highest productivity (12888 U l(-1) h(-1)), which is 13.6-fold higher than the DO-based strategy.