A simple structured model for recombinant IDShr protein production in Pichia pastoris

A simple structured model is proposed for the methanol production phase of the iduronate 2-sulphate sulfatase recombinant enzyme (IDShr) in Pichia patoris Mut(+). The model is mainly focused in oxidative stress phenomenon due to methanol consumption and based on extracellular experimental information and the basic knowledge of methanol metabolism in Pichia pastoris yeast (P. pastoris). The model's prediction shows a reasonable accuracy as compared with the experimental data. Likewise, it was proved that this model is able to simulate the production of other recombinant protein in P. pastoris.     

Impact of methanol concentration on secreted protein production in oxygen-limited cultures of recombinant Pichia pastoris

The methylotrophic yeast Pichia pastoris is a powerful system for production of recombinant proteins, showing high ability to secrete properly folded proteins. A major plus is the strong AOX1 promoter highly induced by methanol. During growth on methanol, however, oxygen readily becomes limiting. In oxygen-limited cultivations of recombinant Pichia pastoris, the methanol concentration had a strong impact on the production of a single-chain antibody fragment (scFv). High methanol concentrations were required to compensate the lack of oxygen and fully induce recombinant protein production, at the same time reducing gratuitous biomass formation due to a lower biomass yield. Product concentrations of 60, 150, and 350 mg/L were obtained with methanol concentrations of 0.3, 1, and 3% (v/v). Moreover, accumulation of a putative product fragment that cannot be removed during affinity purification was prevented at high methanol concentrations. Cell vitality after 100 h was maintained above 98% and 96% of the culture with 0.3% and 3% methanol, respectively. In cultivations supplemented with oxygen, in contrast, methanol concentration between 0.3% and 3% did not influence the product yield of 300-400 mg/L. Thus, efficient recombinant protein production under oxygen-limitation seems to require high methanol concentrations, enabling product concentration as high as otherwise obtained only with expensive supply of pure oxygen.     

Expression, purification, and activity identification of Alfimeprase in Pichia pastoris

Alfimeprase (ALF) is a truncated form of non-hemorrhagic zinc metalloproteinase fibrolase. In order to achieve a high level secretion and full activity expression of ALF, the Pichia pastoris (P. pastoris) expression system was used. ALF coding sequence fused with a 6 *histidine tag and an enterokinase recognition site at the N-terminus was cloned into the expression vector pPIC9K and then expressed in P. pastoris strains of GS115 and KM71 by methanol induction. SDS-PAGE and Western blotting analysis showed that the secreted recombinant ALF (rALF) had a molecular weight of 23.8 kDa and was bound specifically to mouse anti-His. tag monoclonal antibody. Under the optimized culture parameters of pH value, initial A(600) value, methanol daily addition concentration and induction time length, the production of rALF reached up to 510 mg/L and 465 mg/L of the GS115 and KM71 transformants, respectively. It also appeared that KM71 was producing a more pure protein than GS115 while GS115 was producing more rALF per unit volume. Through one-step affinity chromatography, the purity of rALF was as high as 96%. The fibrinolytic activity of rALF revealed by the modified fibrin plate method indicated that the protein was efficiently secreted and functionally expressed, and thrombolysis of rALF was demonstrated to be dose-dependent and time-relative. The improved expression system will facilitate further studies and industrial production of ALF.     

不同甲醇流加策略对重组毕赤醇母高密度发酵生产水蛭素的影响

考察了不同甲醇流加策略对毕赤酵母高密度发酵生产水蛭素的影响。溶氧控制法不能有效地防止甲醇的过量流加。气相色谱离线检测法虽然防止了甲醇流加过量 ,但甲醇浓度的波动较大。利用甲醇传感器在线检测控制甲醇的流加可维持较恒定的甲醇浓度。在流加甲醇的同时 ,以限制性速率流加甘油可以增加表达期间的能量供应 ,提高产物的表达量。经优化后 ,采用甲醇甘油混合流加时细胞干重达到 16 2g L ,水蛭素活性达到 2 4×10 4ATU mL ,即 1 7g L。     

甲醇浓度对毕赤酵母表达重组人复合α干扰素分离纯化得率的影响

研究了毕赤酵母Pichia pastoris表达的重组人复合α干扰素(cIFN)时不同诱导甲醇浓度对cIFN分离纯化得率的影响,并分析了原因.在5L罐中采用0.25、0.50和0.75％(W/V)三个甲醇浓度诱导时,在0.75％高甲醇浓度诱导下cIFN表达水平最高,达到2.06 g/L,是0.25％低甲醇浓度诱导的1.24倍,但是低甲醇浓度诱导下cIFN分离纯化得率却高于高甲醇诱导浓度下3.75倍.另外,低甲醇浓度下发酵上清液cIFN抗病毒活性为2.85×108IU/mL,较高甲醇浓度提高了4.48倍.进一步采用SDS-PAGE和Native-PAGE免疫印迹分析不同条件下发酵液中cIFN存在状态,发现在高甲醇浓度下cIFN容易形成大量的聚合体,分别为共价聚合和非共价聚合,而cIFN单体含量较少,但是低甲醇浓度诱导下情况完全相反.最终在0.25％甲醇诱导下分离纯化1L发酵上清液可得0.73 g单体cIFN,是0.75％甲醇诱导下的3.84倍.     

Design of a novel automated methanol feed system for pilot-scale fermentation of Pichia pastoris

Large-scale fermentation of Pichia pastoris requires a large volume of methanol feed during the induction phase. However, a large volume of methanol feed is difficult to use in the processing suite because of the inconvenience of constant monitoring, manual manipulation steps, and fire and explosion hazards. To optimize and improve safety of the methanol feed process, a novel automated methanol feed system has been designed and implemented for industrial fermentation of P. pastoris. Details of the design of the methanol feed system are described. The main goals of the design were to automate the methanol feed process and to minimize the hazardous risks associated with storing and handling large quantities of methanol in the processing area. The methanol feed system is composed of two main components: a bulk feed (BF) system and up to three portable process feed (PF) systems. The BF system automatically delivers methanol from a central location to the portable PF system. The PF system provides precise flow control of linear, step, or exponential feed of methanol to the fermenter. Pilot-scale fermentations with linear and exponential methanol feeds were conducted using two Mut(+) (methanol utilization plus) strains, one expressing a recombinant therapeutic protein and the other a monoclonal antibody. Results show that the methanol feed system is accurate, safe, and efficient. The feed rates for both linear and exponential feed methods were within ± 5% of the set points, and the total amount of methanol fed was within 1% of the targeted volume.     

细极链格孢菌peaT2基因在毕赤酵母中的表达及蛋白功能确定

从细极链格孢菌表达文库获得阳性克隆子,序列分析表明,克隆的DNA片段中含有完整的开放阅读框架,将该基因命名为peaT2(GenBank登录号为EF212880)。用PCR法扩增peaT2基因的编码序列并亚克隆到毕赤酵母表达系统的表达载体pPIC9K上,得到重组质粒pPIC9K/peaT2。重组质粒经SacⅠ线性化后用电穿孔法导入到毕赤酵母(Pichia pastoris)GS115中,采用MD、G418-YPD平板和PCR法筛选Mut+表型,获得了分泌表达的重组毕赤酵母。随机挑取一菌株作为表达菌,用甲醇诱导PeaT2蛋白表达。SDS-PAGE及Western blot检测结果均表明PeaT2在毕赤酵母中成功地分泌表达。用peaT2基因的表达蛋白处理小麦种子,生物测定表明,表达蛋白能明显促进小麦的生长,具有蛋白激发子作用。     

On-line monitoring and control of methanol concentration in shake-flask cultures of Pichia pastoris

The methylotrophic yeast Pichia pastoris can be used to express recombinant genes at high levels under the control of the methanol-inducible alcohol oxidase 1 (AOX1) promoter. Accurate regulation of the methanol concentration in P. pastoris cultures is necessary to maintain induction, while preventing accumulation of methanol to cytotoxic levels. We developed an inexpensive methanol sensor that uses a gas-permeable silicone rubber tube immersed in the culture medium and an organic solvent vapor detector. The sensor was used to monitor methanol concentration continuously throughout a fed-batch shake-flask culture of a P. pastoris clone producing the N-lobe of human transferrin. The sensor calibration was stable for the duration of the culture and the output signal accurately reflected the methanol concentration determined off-line by HPLC. A closed-loop control system utilizing this sensor was developed and used to maintain a 0.3% (v/v) methanol concentration in the culture. Use of this system resulted in a fivefold increase in volumetric protein productivity over levels obtained using the conventional fed-batch protocol. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 279-286, 1997.     

Recombinant shrimp (Litopenaeus vannamei) trypsinogen production in Pichia pastoris

Shrimp (Litopenaeus vannamei) trypsinogen has never been isolated from its natural source. To assess the production of L. vannamei trypsinogen, we engineered Pichia pastoris strains and evaluated two culture approaches with three induction culture media, to produce recombinant shrimp trypsinogen for the first time. The trypsinogen II cDNA was fused to the signal sequence of the Saccharomyces cerevisiae alpha mating factor, placed under the control of the P. pastoris AOX1 promoter, and integrated into the genome of P. pastoris host strain GS115. Using standard culture conditions for heterologous gene induction of a GS115 strain in shake flasks, recombinant shrimp trypsinogen was not detected by SDS‐PAGE and Western blot analysis. Growth kinetics revealed a toxicity of recombinant shrimp trypsinogen or its activated form over the cell host. Thus, a different culture approach was tested for the induction step, involving the use of high cell density cultures, a higher frequency of methanol feeding (every 12 h), and a buffered minimal methanol medium supplemented with sorbitol or alanine; alanine supplemented medium was found to be more efficient. After 96 h of induction with alanine supplemented medium, a 29‐kDa band from the cell‐free culture medium was clearly observed by SDS‐PAGE, and confirmed by Western blot to be shrimp trypsinogen, at a concentration of 14 μg/mL. Our results demonstrate that high density cell cultures with alanine in the induction medium allow the production of recombinant shrimp trypsinogen using the P. pastoris expression system, because of improved cell viability and greater stability of the recombinant trypsinogen. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

双碳源流加对重组毕赤酵母高效表达葡萄糖氧化酶的影响

葡萄糖氧化酶(GOD)是一种具有广泛应用前景的工业酶.为了实现葡萄糖氧化酶的高效生产,提高重组毕赤酵母生产GOD的产量和增强生产强度,对重组毕赤酵母诱导阶段的初始菌体浓度和甲醇浓度进行了优化.在此基础上,诱导期采用了双碳源(甘油、山梨醇和甘露醇)与甲醇混合流加的模式.研究发现,最佳诱导前初始菌体浓度和甲醇浓度分别为100 g/L和18 g/L,此时GOD产量为427.6 U/mL.在诱导阶段采用甘油、山梨醇和甘露醇与甲醇的混合添加均可以提高GOD产量,其中甘露醇与甲醇的混合流加效果最为显著.当甲醇与甘露醇混合流加的比例为20∶1(W/W)时,诱导156h GOD产量和生产强度分别可达711.3 U/mL和4.60 U/(mL·h),比甲醇单一流加策略结果分别提高了66.3％和67.9％.此外采用合适的甘露醇混合流加策略不但不会抑制AOX1启动子的表达,甚至有一定促进作用,AOX酶活性为8.8 U/g(对照为5.2 U/g).双碳源流加方式还能推广到毕赤酵母其他表型中,为该系统高效表达外源蛋白提供一种新策略.     

重组毕赤酵母产青霉素G酰化酶的分批发酵动力学研究

构建了重组毕赤酵母产青霉素G酰化酶的分批发酵动力学模型。实验考察了分批发酵过程中甘油消耗、甲醇浓度、菌体浓度、溶氧、补料时间对青霉素G酰化酶活力的影响。应用Matlab软件,对菌体生长、基质消耗和产物生成方程进行最优参数估算和非线性拟合,得到相应的动力学模型。模型的计算值与实验值能较好地拟合,表明所建模型能较好反映重组毕赤酵母产青霉素G酰化酶的分批发酵过程。     

Fermentation strategies for improved heterologous expression of laccase in Pichia pastoris

Improved expression of recombinant laccase by Pichia pastoris carrying the lcc1 cDNA isolated from Trametes versicolor was achieved by optimization of the cultivation conditions in a fermentor equipped with a methanol sensor system. The results indicated that the activity obtained in fermentor cultivations was at least 7 times higher than in shake-flask cultures. Three different strategies for fermentor cultivations were compared: A (30 degrees C, 1.0% methanol), B (20 degrees C, 1.0% methanol), and C (20 degrees C, 0.5% methanol). The laccase activity, particularly the specific activity, could be improved by decreasing the cultivation temperature. The mechanisms behind the temperature effect on the laccase activity may be ascribed to poor stability, release of more proteases from dead cells, and folding problems at higher temperature. The results showed that the methanol concentration had a marked effect on the production of active heterologous laccase. A fivefold higher volumetric laccase activity was obtained when the methanol concentration was kept at 0.5% instead of 1.0%. The detrimental effect of methanol on the production of recombinant laccase may be attributed to lower laccase stability, a higher proteolytic activity, and folding problems due to higher growth rate at 1.0% methanol.     

重组人小分子抗体ScFv-Fc发酵条件的优化及纯化

目的:研究重组人小分子抗体ScFv-Fc在毕赤酵母中分泌表达的最佳条件,以及ScFv-Fc的纯化方法。方法:分别从甲醇浓度、pH、诱导时间等方面对毕赤酵母重组菌株产生ScFv-Fc的发酵过程进行了优化;通过硫酸铵沉淀结合protein A亲和层析柱,对ScFv-Fc的纯化方法进行了研究。结果:确定ScFv-Fc在毕赤酵母中分泌表达的最佳条件为:在pH5.2的条件下,以0.5%甲醇诱导72 h。经过protein A亲和层析柱纯化后,ScFv-Fc纯度可达94%以上。结论:确定了ScFv-Fc在毕赤酵母中分泌表达的最佳条件以及纯化方法,为重组抗体分子诊断、治疗试剂的开发以及抗体的人源化奠定了物质基础。     

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.     

重组毕赤酵母生产β-葡萄糖苷酶发酵条件初步研究

为提高重组毕赤酵母(P.pastoris KM71/pPIC9K-bgl)生产β-葡萄糖苷酶的产量,在摇瓶条件下对重组P.pastoris产β-葡萄糖苷酶的发酵过程进行了优化,得到最佳的条件:生长阶段甘油浓度为30 g/L,接种量为10%,诱导阶段甲醇的初浓度为4%,过程补加甲醇0.5%,诱导温度30℃,pH7.5,诱导周期120 h,酶活可达到245 U/mL。在此基础上,在3 L发酵罐上进行初步放大,流加甘油提高细胞密度至OD_(600)为170,开始流加甲醇诱导,最终BGL酶活达到1 175 U/mL。比摇瓶提高了4.8倍,为β-葡萄糖苷酶工业化生产打下了坚实的基础。     

Increasing secretion of a bivalent anti-T-cell immunotoxin by Pichia pastoris

The bivalent anti-T-cell immunotoxin A-dmDT390-bisFv(G(4)S) was developed for treatment of T-cell leukemia and autoimmune diseases and for tolerance induction for transplantation. This immunotoxin was produced extracellularly in toxin-sensitive Pichia pastoris JW102 (Mut(+)) under control of the AOX1 promoter. There were two major barriers to efficient immunotoxin production, the toxicity of the immunotoxin for P. pastoris and the limited capacity of P. pastoris to secrete the immunotoxin. The immunotoxin toxicity resulted in a decrease in the methanol consumption rate, cessation of cell growth, and low immunotoxin productivity after the first 22 h of methanol induction. Continuous cell growth and continuous immunotoxin secretion after the first 22 h of methanol induction were obtained by adding glycerol to the methanol feed by using a 4:1 methanol-glycerol mixed feed as an energy source and by continuously adding a yeast extract solution during methanol induction. The secretory capacity was increased from 22.5 to 37 mg/liter by lowering the induction temperature. A low temperature reduced the methanol consumption rate and protease activity in the supernatant but not cell growth. The effects of adding glycerol and yeast extract to the methanol feed were synergistic. Adding yeast extract primarily enhanced methanol utilization and cell growth, while adding glycerol primarily enhanced immunotoxin production. The synergy was further enhanced by decreasing the induction temperature from 23 to 15 degrees C, which resulted in a robust process with a yield of 37 mg/liter, which was sevenfold greater than the yield previously reported for a toxin-resistant CHO cell expression system. This methodology should be applicable to other toxin-related recombinant proteins in toxin-sensitive P. pastoris.     

Intracellular expression of Vitreoscilla hemoglobin improves S-adenosylmethionine production in a recombinant Pichia pastoris

To develop an efficient way to produce S-adenosylmethionine (SAM), methionine adenosyltransferase gene (mat) from Streptomyces spectabilis and Vitreoscilla hemoglobin gene (vgb) were coexpressed intracellularly in Pichia pastoris, both under control of methanol-inducible promoter. Expression of mat in P. pastoris resulted in about 27 times higher specific activity of methionine adenosyltransferase (SMAT) and about 19 times higher SAM production relative to their respective control, suggesting that overexpression of mat could be used as an efficient method for constructing SAM-accumulating strain. Under induction concentration of 0.8 and 2.4% methanol, coexpression of vgb improved, though to different extent, cell growth, SAM production, and respiratory rate. However, the effects of VHb on SAM content (specific yield of SAM production) and SMAT seemed to be methanol concentration-dependent. When cells were induced with 0.8% methanol, no significant effects of VHb expression on SAM content and specific SMAT could be detected. When the cells were induced with 2.4% methanol, vgb expression increased SAM content significantly and depressed SMAT remarkably. We suggested that under our experimental scheme, the presence of VHb might improve ATP synthesis rate and thus improve cell growth and SAM production in the recombinant P. pastoris.     

Pathway analysis of Pichia pastoris to elucidate methanol metabolism and its regulation for production of recombinant proteins

This research rationally analyzes metabolic pathways of Pichia pastoris to study the metabolic flux responses of this yeast under methanol metabolism. A metabolic model of P. pastoris was constructed and analyzed by elementary mode analysis (EMA). EMA was used to comprehensively identify the cell's metabolic flux profiles and its underlying regulation mechanisms for the production of recombinant proteins from methanol. Change in phenotypes and flux profiles during methanol adaptation with varying feed mixture of glycerol and methanol was examined. EMA identified increasing and decreasing fluxes during the glycerol–methanol metabolic shift, which well agreed with experimental observations supporting the validity of the metabolic network model. Analysis of all the identified pathways also led to the determination of the metabolic capacities as well as the optimum metabolic pathways for recombinant protein synthesis during methanol induction. The network sensitivity analysis revealed that the production of proteins can be improved by manipulating the flux ratios at the pyruvate branch point. In addition, EMA suggested that protein synthesis is optimum under hypoxic culture conditions. The metabolic modeling and analysis presented in this study could potentially form a valuable knowledge base for future research on rational design and optimization of P. pastoris by determining target genes, pathways, and culture conditions for enhanced recombinant protein synthesis. The metabolic pathway analysis is also of considerable value for production of therapeutic proteins by P. pastoris in biopharmaceutical applications. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:28–37, 2014     

重组毕赤酵母高密度发酵生产碱性果胶酶的策略

重组Pichia pastoris GS115表达碱性果胶酶的诱导阶段, 最佳初始菌体浓度和甲醇诱导浓度分别为122 g/L和20 g/L, 两者之间最佳比值范围是0.16~0.20 g/g (甲醇/菌体浓度). 在此基础上通过生长阶段甘油的指数流加, 以及诱导阶段基于甲醇比消耗速率和溶氧等参数进行甲醇流加的方式, 将甲醇与菌体浓度比例控制在0.171~0.195 g/g之间. 此时, 酶活达到430 u/mL, 生产强度为4.34 u/mL/h, 实现了碱性果胶酶高效生产。     

重组毕赤酵母高密度发酵生产碱性果胶酶的策略

重组Pichia pastoris GS115表达碱性果胶酶的诱导阶段, 最佳初始菌体浓度和甲醇诱导浓度分别为122 g/L和20 g/L, 两者之间最佳比值范围是0.16~0.20 g/g (甲醇/菌体浓度). 在此基础上通过生长阶段甘油的指数流加, 以及诱导阶段基于甲醇比消耗速率和溶氧等参数进行甲醇流加的方式, 将甲醇与菌体浓度比例控制在0.171~0.195 g/g之间. 此时, 酶活达到430 u/mL, 生产强度为4.34 u/mL/h, 实现了碱性果胶酶高效生产。