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。     

A dynamic fed batch strategy for a Pichia pastoris mixed feed system to increase process understanding

Mixed substrate feeding strategies are frequently investigated to enhance the productivity of recombinant Pichia pastoris processes. For this purpose, numerous fed batch experiments or time-consuming continuous cultivations are required to optimize control parameters such as the substrate mixing ratio and the applied methanol concentration. In this study, we decoupled the feeding of methanol and glycerol in a mixed substrate fed batch environment to gain process understanding for a recombinant P. pastoris Muts strain producing the model enzyme horseradish peroxidase. Specific substrate uptake rates (qs) were controlled separately, and a stepwise increased qGly-control scheme was applied to investigate the effect of various substrate fluxes on the culture. The qs-controlled strategy allowed a parallel characterization of the metabolism and the recombinant protein expression in a fed batch environment. A critical-specific glycerol uptake rate was determined, where a decline of the specific productivity occurred, and a time-dependent acceleration of protein expression was characterized with the dynamic fed batch approach. Based on the observations on recombinant protein expression, propositions for an optimal feeding design to target maximal productivities were stated. Thus, the dynamic fed batch strategy was found to be a valuable tool for both process understanding and optimization of product formation for P. pastoris in a mixed substrate environment.     

Establishing a versatile fermentation and purification procedure for human proteins expressed in the yeasts Saccharomyces cerevisiae and Pichia pastoris for structural genomics

We describe the introduction of the yeasts Saccharomyces cerevisiae and Pichia pastoris as eukaryotic hosts for the routine production of recombinant proteins for a structural genomics initiative. We have previously shown that human cDNAs can be efficiently expressed in both hosts using high throughput procedures. Expression clones derived from these screening procedures were grown in bioreactors and the over-expressed human proteins were purified, resulting in obtaining significant amounts suitable for structural analysis. We have also developed and optimized protocols enabling a high throughput, low cost fermentation and purification strategy for recombinant proteins for both S. cerevisiae and P. pastoris on a scale of 5 to 10 mg. Both batch and fed batch fermentation methods were applied to S. cerevisiae. The fed batch fermentations yielded a higher biomass production in all the strains as well as a higher productivity for some of the proteins. We carried out only fed batch fermentations on P. pastoris strains. Biomass was produced by cultivation on glycerol, followed by feeding methanol as carbon source to induce protein expression. The recombinant proteins were expressed as fusion proteins that include a N-terminal His-tag and a C-terminal Strep-tag. They were then purified by a two-step chromatographic procedure using metal-affinity chromatography and StrepTactin-affinity chromatography. This was followed by gel filtration for further purification and for buffer exchange. This three-step purification procedure is necessary to obtain highly purified proteins from yeast. The purified proteins have successfully been subjected to crystallization and biophysical analysis.     

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。     

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。     

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.     

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.     

Reduced oxygen supply increases process stability and product yield with recombinant Pichia pastoris

A single-chain antibody fragment directed against fimbriae of enterotoxigenic Escherichia coli was produced by recombinant Pichia pastoris under control of the methanol-inducible AOX1 promoter. In high-cell-density cultivation on defined medium, methanol-limited and methanol-saturated conditions were compared. After batch and fed-batch phase on glycerol, the methanol concentration was controlled to 1% (v/v) or methanol was fed with an exponentially increasing rate. Whereas methanol limitation impaired cell integrity and product quality, finally yielding no active product as a result of degradation, oxygen limitation was acceptable. To postpone the onset of limitation, the inlet air was enriched by pure oxygen. Because of faster methanol consumption, however, the process became sensitive to fluctuations in the feeding rate, and complete arrest of metabolism encountered upon small perturbations shortened the active production period. Without additional oxygen supply, the process was robust. Loss of culture integrity was monitored by flow cytometry and was found to precede changes in metabolic rates; it can thus serve as a sensitive indicator of forthcoming problems. Single-step downstream processing from the culture supernatant by His-affinity chromatography was efficient when antifoam agent that coagulates upon pH titration was omitted and yielded 1 g of purified lyophilized product from 6 L initial culture volume.     

内皮细胞抑制素酵母工程菌的高密度发酵及产物纯化和活性分析

用 30升发酵罐研究了内皮细胞抑制素 (EDN)酵母工程菌P .pastorisGS115 (pPIC9K EDN)的高密度发酵工艺 ,摸索出发酵培养基 ,pH ,诱导时间等对菌体生长和基因表达的影响 .根据所确定的最适条件进行发酵 ,通过补料和甲醇诱导 4 8h后 ,工程菌GS115 (pPIC9K EDN)生物量的A60 0 值达到 2 5 0 ,分泌量为 15 0mg L .发酵液经StreamlineSP ,SepharoseSPFF离子交换柱和Sepharose HeparinHiTrap亲和柱纯化 ,产物纯度达 97%以上 ,回收率为 6 0 % .Western印迹结果表明 ,酵母工程菌GS115 (pPIC9K EDN)表达的重组人内皮细胞抑制素具有天然EDN的免疫原性 .MTT法和抑癌实验结果显示 :纯化产物能抑制人脐静脉内皮细胞的增殖并能抑制移植于小鼠的黑色素瘤的生长 ,其平均抑瘤率是 94 2 % .     

Methanol bioconversion by Butyribacterium methylotrophicum--batch fermentation yield and kinetics

Butyribacterium methylotrophicum is an anaerobic bacterium that can convert methanol to butyrate. This ability to produce longer-chain carbon compounds from C(1) substrates could be of commercial significance. The fermentation rates and product formation depend on the methanol/bicarbonate ratios during fermentation. The kinetics of batch fermentation fit the Luedeking-Piret model with growth and maintenance associated product formation. Butyrate yield of 0.256 mol/mol methanol (ca. 85% of theoretical yield) has been obtained in batch fermentation.     

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.     

增加植酸酶基因appA-m的拷贝提高其在巴斯德毕赤酵母的表达量

为了进一步提高植酸酶的发酵效价,降低植酸酶生产成本,对毕赤酵母表达载体pGAPZα-A进行了改造。将表达载体pPIC9的AOX1启动子序列引入pGAPZα-A,使之成为甲醇可诱导型表达载体pAOXZα,插入植酸酶基因appA-m后得到重组载体pAOXZα-appA-m。以染色体上带有一个拷贝的appA-m基因、发酵效价可达到7.5×106IU/mL发酵液的重组酵母菌株74#为受体菌进行转化,在该重组菌株的染色体上的另一位点整合含有植酸酶基因的表达盒,经筛选到高表达植酸酶的重组子。通过PCR进行验证,植酸酶基因被整合到重组酵母的染色体上,且受体菌中原有的植酸酶基因结构未改变。重组菌在5L发酵罐经甲醇诱导120h植酸酶蛋白表达量达到4mg/mL发酵液,酶活性(发酵效价)达到1.2×107IU/mL发酵液以上,较含单拷贝植酸酶基因的受体菌株表达量有较大程度提高。PCR检测及表达量分析证明改良的菌株具有很好的遗传稳定性和表达稳定性。     

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。     

Improving the monitoring of methanol concentration during high cell density fermentation of Pichia pastoris

The Pichia pastoris expression system is widely used for the production of recombinant proteins. A simple and efficient experimental set-up allowing on-line monitoring of the methanol concentration during the fermentation of P. pastoris based on the detection of the methanol vapor concentration in the exhaust air from fermenter by a tin dioxide (SnO2) semiconductor sensor is described. An experimental procedure to allow precise calibration of the system and to reduce methanol sensor's interferences (>95% reduction) are also presented and discussed. Accuracy and measurement error were estimated about 0.05 g x l(-1) and 6%, respectively. The efficient monitoring of methanol will help to advanced control of recombinant protein production and process optimization.     

Improved production of recombinant ovine interferon-tau by mut(+) strain of Pichia pastoris using an optimized methanol feed profile

Recombinant ovine interferon-tau (r-oIFN-tau) production by Pichia pastoris was studied using methanol as the sole carbon source during induction. The cells were grown on glycerol up to a certain cell density before induction of the AOX1 promoter by methanol for expression of the recombinant protein. Cell growth on methanol has been modeled using a substrate-feed equation, which served as the basis for an effective computer control of the process. The r-oIFN-tau concentration in the culture began to decline despite continued cell growth after 50 (+/- 6) h of induction, which was associated with an increase in proteolytic activity of the fermentation broth. A specific growth rate of 0.025 h(-1) was found to be optimal for r-oIFN-tau production. No significant improvement in r-oIFN-tau production was observed when the specific growth rate was stepped up before the critical point when r-oIFN-tau concentration started decreasing during fermentation. However, best results were obtained when the specific growth rate was stepped down from 0.025 to 0.02 h(-1) at 38 h of induction, whereby the active production period was prolonged until 70 h of induction and the broth protease activity was correspondingly reduced. The corresponding maximum protein yield was 391.7 mg x L(-1) after 70 h of fermentation. The proteolytic activity could be reduced by performing fermentations at specific growth rates of 0.025 h(-1) or below. The recombinant protein production can be performed at an optimal yield by directly controlling the methanol feed rate by a computer-controlled model. The production profile of r-oIFN-tau was found to be significantly different from other secreted and intracellular recombinant protein processes, which is an indication that recombinant protein production in Pichia pastoris needs to be optimized as individual processes following established principles.     

Quantitative physiology of Pichia pastoris during glucose‐limited high‐cell density fed‐batch cultivation for recombinant protein production

Pichia pastoris has become one of the major microorganisms for the production of proteins in recent years. This development was mainly driven by the readily available genetic tools and the ease of high‐cell density cultivations using methanol (or methanol/glycerol mixtures) as inducer and carbon source. To overcome the observed limitations of methanol use such as high heat development, cell lysis, and explosion hazard, we here revisited the possibility to produce proteins with P. pastoris using glucose as sole carbon source. Using a recombinant P. pastoris strain in glucose limited fed‐batch cultivations, very high‐cell densities were reached (more than 200 g_CDW L^?1) resulting in a recombinant protein titer of about 6.5 g L^?1. To investigate the impact of recombinant protein production and high‐cell density fermentation on the metabolism of P. pastoris, we used ¹³C‐tracer‐based metabolic flux analysis in batch and fed‐batch experiments. At a controlled growth rate of 0.12 h^?1 in fed‐batch experiments an increased TCA cycle flux of 1.1 mmol g^?1 h^?1 compared to 0.7 mmol g^?1 h^?1 for the recombinant and reference strains, respectively, suggest a limited but significant flux rerouting of carbon and energy resources. This change in flux is most likely causal to protein synthesis. In summary, the results highlight the potential of glucose as carbon and energy source, enabling high biomass concentrations and protein titers. The insights into the operation of metabolism during recombinant protein production might guide strain design and fermentation development. Biotechnol. Bioeng. 2010;107: 357–368. © 2010 Wiley Periodicals, Inc.     

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。     

流式细胞术检测毕赤酵母发酵过程中胞内活性氧水平

以2′,7′-二氢二氯荧光黄双乙酸钠(DCFH-DA)和碘化丙锭(PI)为标记探针,通过DCFH-DA/PI双染色与PI单染色的对照,检测毕赤酵母胞内活性氧(reactive oxygen species,ROS)的水平及其影响。研究发现发酵过程细胞活性下降与胞内ROS积累相关。在甘油生长期,细胞几乎没有ROS积累,细胞活性接近100%。在甲醇诱导初期,部分细胞积累少量的ROS,细胞活性仍然很高,死亡细胞所占比例只有1.5%。在甲醇诱导后期,94.0%的细胞积累了大量的ROS,高含量的ROS造成细胞损伤,引起部分细胞丧失了活性,在总共29.1%的死亡细胞中,高ROS积累的死亡细胞占了25.4%。     

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.     

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。