Causes of proteolytic degradation of secreted recombinant proteins produced in methylotrophic yeast Pichia pastoris: case study with recombinant ovine interferon-tau

It was observed that during fermentative production of recombinant ovine interferon-tau (r-oIFN-tau) in Pichia pastoris, a secreted recombinant protein, the protein was degraded increasingly after 48 h of induction and the rate of degradation increased towards the end of fermentation at 72 h, when the fermentation was stopped. Proteases, whose primary source was the vacuoles, was found in increasing levels in the cytoplasm and in the fermentation broth after 48 h of induction and reached maximal values when the batch was completed at 72 h. Protease levels at various cell fractions as well as in the culture supernatant were lower when glycerol was used as the carbon source instead of methanol. It can be concluded that methanol metabolism along with cell lysis towards the end of fermentation contributes to increased proteolytic activity and eventual degradation of recombinant protein.     

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。     

以葡萄糖为生长相基质的重组毕赤酵母表达植酸酶发酵

甲醇营养型毕赤酵母表达外源蛋白是在醇氧化酶（alcohol oxidase,AOX）启动子（PAOXI）严格调控下进行的,然而这种启动子在转录水平受到葡萄糖的阻遏。本文研究了毕赤酵母在葡萄糖替代甘油为生长相碳源时表达重组植酸酶蛋白的发酵特征。结果表明：初始葡萄糖浓度为20dL的细胞得率高,为0．39g[DCW]／g。通过基于实时参数（溶氧和呼吸商）调控的葡萄糖补料策略,生长相40h后细胞密度达到100g[DCW]／L,甲醇诱导100h后植酸酶产量达到2200FTUphytase／mL,甲醇得率系数为0．25FTU phytase／gmethnol。因此,在毕赤酵母高表达重组蛋白培养中葡萄糖能够用作生长相基质,并能实现重组蛋白的高效表达。     

人源性抗HBsAg Fab抗体的发酵生产研究

为了适应工业生产的需要,利用fed—batch方法,重组人源性抗HBsAg Fab抗体酵母工程菌在30L发酵罐中进行了高密度发酵,发酵最适温度30℃,pH值范围5．0～5．3,溶氧范围20％～30％。发酵液OD600值达到300时开始诱导,甲醇最佳诱导浓度为10mL／L。重组人源性抗HBsAg Fab抗体经离子交换层析纯化,纯化产品经SDS-PAGE、Western blot进行分析和ELISA方法进行活性测定。结果显示,重组Fab抗体在Fed-batch发酵系统中可高效表达,经过192h的发酵生产,重组人源性抗HBsAg Fab抗体的表达量可达412mg／L。发酵上清经过离子交换层析纯化,获得纯度为95％的重组Fab抗体,该Fab抗体经ELISA分析具有较高的HBsAg抗原亲和力和特异性。结果证实可以通过高密度发酵毕赤酵母工程菌来高效生产重组人源性抗HBsAg Fab抗体,为后续的工业化生产应用奠定了基础。     

毕赤酵母表达重组人白细胞介素11的连续培养研究

对毕赤酵母表达重组人白细胞介素11(rhIL11)工程菌的连续培养进行了工艺研究。连续培养在10L工作体积的发酵罐中进行,整个发酵过程历时约20天,发酵上清中rhIL11表达浓度约400mgml。在稀释率D=005h下,菌浓OD600达到100以上。     

重组人干扰素ω在对数生长期毕赤酵母中的高效表达特性研究

用不同比生长速率μ的毕赤酵母探讨其表达外源重组蛋白的差异性,通过起始pH值、甲醇诱导浓度和周期、菌体浓度、装液量等实验,优化具有较高μ的对数生长期毕赤酵母表达rhIFNω的摇瓶条件。结果表明,μ对毕赤酵母表达rhIFNω有显著影响。μ为0.1612h-1的毕赤酵母表达rhIFNω最高为558mg/L,较μ为0.1321、0.0505和0.0052h-1的毕赤酵母分别提高50%、68%和99%。对数生长期的毕赤酵母表达rhIFNω的最适摇瓶表达条件为:250mL摇瓶装入30mL BMMY,控制菌体浓度达到200~300g/L(WCW),起始pH值自然,每24h添加甲醇15g/L一次,诱导表达周期为4d。通过表达条件的优化,rhIFNω的表达量达到1070mg/L,较优化前提高149%。     

甲醇抑制时重组毕赤酵母发酵的特性研究

本文对毕赤酵母进行了恒化培养研究。以甲醇为唯一碳源时,在稀释率较低时(D<0.048 h^-1),连续培养系统操作很稳定。但在稀释率高时(D>0.048h^-1),连续培养系统的定态点不止一个,实验不能维持,故采用比生长速率恒定的分批流加培养进行研究。结果表明,毕赤酵母的生长符合Andrew普遍化底物抑制模型。综合考虑水蛭素的生成、底物的消耗,在生产中维持甲醇浓度为限制性浓度(0.5 g/L),且维持比生长速率为0.02 h^-1时,水蛭素Hir65的比生成速率达到最大值0.2 mg/(g·h)且甲醇的比消耗速率为0.04 g/(g·h)。     

电子嗅在线反馈控制毕赤酵母糖化酶发酵过程中甲醇浓度新方法的应用

探索了电子嗅传感仪直接通过发酵尾气进行发酵液中甲醇浓度在线检测的方法,建立了毕赤酵母表达糖化酶过程中甲醇浓度的自动化反馈补料控制模型,可准确实现发酵过程中甲醇浓度的精确控制;研究表明,当利用电子嗅将培养液中甲醇浓度稳定控制在(890±35)ppm水平下,发酵诱导培养到128h时目的蛋白糖化酶酶活达到了8 153U/ml,与甲醇浓度控制在(350±26)ppm时的发酵水平相比提升了48.8%。该方法具有无需前处理、与发酵液非接触、快速和准确性的优点,为提升工程酵母在工业发酵培养过程工艺的优化控制具有重要的指导作用。     

Cell bank characterization and fermentation optimization for production of recombinant heavy chain C-terminal fragment of botulinum neurotoxin serotype E (rBoNTE(H(c)): antigen E) by Pichia pastoris

A process was developed for production of a candidate vaccine antigen, recombinant C-terminal heavy chain fragment of the botulinum neurotoxin serotype E, rBoNTE(H(c)) in Pichia pastoris. P. pastoris strain GS115 was transformed with the rBoNTE(H(c)) gene inserted into pHILD4 Escherichia coli-P. pastoris shuttle plasmid. The clone was characterized for genetic stability, copy number, and BoNTE(H(c)) sequence. Expression of rBoNTE(H(c)) from the Mut(+) HIS4 clone was confirmed in the shake-flask, prior to developing a fed-batch fermentation process at 5 and 19 L scale. The fermentation process consists of a glycerol growth phase in batch and fed-batch mode using a defined medium followed by a glycerol/methanol transition phase for adaptation to growth on methanol and a methanol induction phase resulting in the production of rBoNTE(H(c)). Specific growth rate, ratio of growth to induction phase, and time of induction were critical for optimal rBoNTE(H(c)) production and minimal proteolytic degradation. A computer-controlled exponential growth model was used for process automation and off-gas analysis was used for process monitoring. The optimized process had an induction time of 9 h on methanol and produced up to 3 mg of rBoNTE(H(c)) per gram wet cell mass as determined by HPLC and Western blot analysis.     

Analysis of single-chain antibody production in Pichia pastoris using on-line methanol control in fed-batch and mixed-feed fermentations.

In the last few years the Pichia pastoris expression system has been gaining more and more interest for the expression of recombinant proteins. Many groups have employed fermentation technology in their investigations because the system is fairly easy to scale up and suitable for the production in the milligram to gram range. A large number of heterologous proteins from different sources has been expressed, but the fermentation process technology has been investigated to a lesser extent. A large number of fermentations are carried out in standard bioreactors that may be insufficiently equipped to meet the demands of high-cell-density fermentations of methylotrophic yeasts. In particular, the lack of on-line methanol analysis leads to fermentation protocols that may impair the optimal expression of the desired products. We have used a commercially available methanol sensor to investigate in detail the effects of supplementary glycerol feeding while maintaining a constant methanol concentration during the induction of a Mut(+) strain of Pichia pastoris. Specific glycerol feed rates in the range of 38-4.2 mg. g(-1). h(-1) (mg glycerol per gram fresh weight per hour) were investigated. Expression of the recombinant scFv antibody fragment was only observed at specific feed rates below 6 mg. g(-1). h(-1). At low specific feed rates, growth was even lower than with methanol as the sole carbon source and the harvest expression level of the scFv was only half of that found in the control fermentation. These results show that glycerol inhibits expression driven by the AOX1 promoter even at extremely limited availability and demonstrate the benefits of on-line methanol control in Pichia fermentation research.     

巴曲酶在毕赤酵母中的高效表达

目的研究巴曲酶在毕赤酵母菌中的表达。方法按Pichiapastoris偏好密码子人工合成巴曲酶全基因,克隆到酵母分泌型表达载体pPICZaA中,将重组载体酶切线性化后经电转化转入X-33。筛选鉴定转化子．经摇瓶发酵甲醇诱导,酵母菌分泌表达有凝血活性的巴曲酶。经SDS-PAGE电泳确定其分子量为33．0 kDa．免疫印迹证明重组巴曲酶具有天然巴曲酶的免疫活性。结果经发酵条件的优化．发酵罐的表达量达到25000Ku／L发酵液。从每升发酵液中可纯化出11．0mg重组巴曲酶。结论巴曲酶毕氏酵母菌成功的构建．为重组巴曲酶止血药的开发奠定了基础。     

发酵条件对毕赤酵母表达重组人干扰素ω糖基化的影响

发酵条件是影响毕赤酵母 (P .pastoris)表达外源重组糖蛋白时糖基化的重要因素。通过菌体浓度、起始pH值、甲醇诱导浓度和周期、装液量等摇瓶发酵实验 ,研究不同发酵条件对毕赤酵母表达分泌型重组人干扰素ω(rhIFNω)过程中糖基化的影响 ;同时 ,在连续培养过程中考察pH值变化对rhIFNω糖基化的影响和分批发酵过程中rhIFNω糖基化的变化。结果表明 ,控制菌体密度 250g L(WCW)、起始pH值 6 0、装液量小于 30mL、甲醇诱导浓度 15g L、甲醇诱导 3次 (每 24h诱导一次 )等发酵条件 ,有利于摇瓶发酵过程中rhIFNω的糖基化 ;控制pH值 70～75可促进rhIFNω的糖基化 ;分批发酵过程中 ,糖基化与非糖基化rhIFNω的含量有同比变化趋势 ,但糖基化rhIFNω所占比例明显低于摇瓶发酵实验的结果 ,其原因有待进一步研究。     

Human chymotrypsinogen B production with Pichia pastoris by integrated development of fermentation and downstream processing. Part 1. Fermentation

Based on an integrated approach of genetic engineering, fermentation process development, and downstream processing, a fermentative chymotrypsinogen B production process using recombinant Pichia pastoris is presented. Making use of the P. pastoris AOX1-promotor, the demand for methanol as the single carbon source as well as an inducer of protein secretion enforced the use of an optimized feeding strategy by help of on-line analysis and an advanced controller algorithm. By using an experimental system of six parallel sparged column bioreactors, proteolytic product degradation could be minimized while also optimizing starting conditions for the following downstream processing. This optimization of process conditions resulted in the production of authentic chymotrypsinogen at a final concentration level of 480 mg.L(-)(1) in the whole broth and a biomass concentration of 150 g.L(-)(1) cell dry weight, thus comprising a space-time yield of 5.2 mg.L(-)(1).h(-)(1). Alternatively to the high cell density fermentation approach, a continuous fermentation process was developed to study the effects of reduced cell density toward oxygen demand, cooling energy, and biomass separation. This development led to a process with a highly increased space-time yield of 25 mg.L(-)(1).h(-)(1) while reducing the cell dry weight concentration from 150 g.L(-)(1) in fed-batch to 65 g.L(-)(1) in continuous cultivation.     

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。     

来源于Escherichia coli的高比活植酸酶基因的高效表达

高效表达高比活植酸酶是进一步提高植酸酶发酵效价、降低植酸酶生产成本的一个有效途径。对源于Escherichiacoli的高比活植酸酶基因appA ,按照毕赤酵母 (Pichiapastoris)密码子的偏爱进行了密码子优化改造。该改造后的基因appA m按正确的阅读框架融合到毕赤酵母表达载体pPIC9上的α 因子信号肽编码序列 3′端 ,通过电击转化得到重组转化子。对重组毕赤酵母的Southernblotting分析证实植酸酶基因已整合到酵母基因组中 ,并确定了整合基因的拷贝数。Northernblotting分析证实植酸酶基因得到了正常转录。SDS PAGE分析和表达产物的研究表明 ,植酸酶得到了高效分泌表达 ,在 5L发酵罐中植酸酶蛋白表达量达到 2 5mg mL发酵液 ,酶活性 (发酵效价 )达到 7 5× 10 6 IU mL发酵液以上 ,大大高于目前报道的各种植酸酶基因工程菌株的发酵效价。     

Maximizing recombinant human serum albumin production in a Muts Pichia pastoris strain

Human serum albumin (HSA) is a cysteine rich molecule that is most abundant in human blood plasma. To remain viable in the market due to lower marketing costs for HSA, it is important to produce a large quantity in an economical manner by recombinant technology. The objective of this study was to maximize recombinant HSA (rHSA) production using a Mut^s Pichia pastoris strain by fermentation process optimization. We evaluated the impact of process parameters on the production of rHSA, including induction cell density (wet cell weight, g/L) and the control of specific growth rate at induction. In this study, we demonstrated that induction cell density is a critical factor for high level production of rHSA under controlled specific growth rate. We observed higher specific productivities at higher induction cell densities (285 g/L) and at lower specific growth rates (0.0022–0.0024/h) during methanol induction phase, and achieved the broth titer of rHSA up to 10 g/L. The temperature shift from 24 to 28^oC was effective to control the specific growth rate at low level (≤0.0024/h) during methanol induction phase while maintaining high specific productivity [0.0908 mg_rHSA/(g_wcw h)]. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1488–1496, 2014     

毕赤酵母高密度发酵工艺的研究

高密度发酵是毕赤酵母提高蛋白表达量的一种重要策略,发酵工艺是高密度发酵的一个重要因素。采用下列措施均可以有效地提高表达水平：调节基础培养基,采用变pH和变温发酵,提高DO,选择最适的诱导前菌体密度和比生长速率并降低甘油初始浓度和采用分段式指数流加进行调控。选择合适的甲醇补料策略：甲醇限制补料（MLFB）、氧气限制补料（OLFB）、甲醇不限制补料（MNLFB）和温度限制补料（TLFB）。采用两种方式调控补料：诱导阶段菌体生长时,甲醇比消耗速率(qMeOH)为0.02-0.03gg-1h-1,而菌体不生长时,qMeOH采用较高值。     

Production of enzymatically active recombinant full-length barley high pI alpha-glucosidase of glycoside family 31 by high cell-density fermentation of Pichia pastoris and affinity purification

Recombinant barley high pI alpha-glucosidase was produced by high cell-density fermentation of Pichia pastoris expressing the cloned full-length gene. The gene was amplified from a genomic clone and exons (coding regions) were assembled by overlap PCR. The resulting cDNA was expressed under control of the alcohol oxidase 1 promoter using methanol induction of P. pastoris fermentation in a Biostat B 5 L reactor. Forty-two milligrams alpha-glucosidase was purified from 3.5 L culture in four steps applying an N-terminal hexa-histidine tag. The apparent molecular mass of the recombinant alpha-glucosidase was 100 kDa compared to 92 kDa of the native barley enzyme. The secreted recombinant enzyme was highly stabile during the 5-day fermentation and had significantly superior specific activity of the enzyme purified previously from barley malt. The kinetic parameters Km, Vmax, and kcat were determined to 1.7 mM, 139 nM x s(-1), and 85 s(-1) using maltose as substrate. This work presents the first production of fully active recombinant alpha-glucosidase of glycoside hydrolase family 31 from higher plants.     

人甲状旁腺激素-血清白蛋白融合蛋白的构建及在毕赤酵母中的表达

利用重叠PCR技术拼接PTH和HSA基因,并将构建好的融合基因插入到载体pUC19测序后插入表达载体pPIC9K中,在启动子AOXⅠ和α交配因子信号肽的作用下,分泌表达融合蛋白PTH-HSA。重组质粒pPIC9K/PTH-HSA经SalⅠ线性化后,电击转化毕赤酵母KM71,经G418筛选得到的转化子。PCR鉴定后,用甲醇诱导表达,蛋白电泳分析表明融合基因得到表达; Western blot分析表明发酵液上清中表达的融合蛋白PTH-HSA具有HSA的抗原性:用酶标法测定发酵上清中融合蛋白的甲状旁腺激素活性为318IU/ml