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.     

混合碳源流加对重组毕赤酵母生产碱性果胶酶的影响

为提高重组毕赤酵母生产碱性果胶酶(PGL)的产量和生产强度,在诱导期采用多种碳源与甲醇混合添加的模式。实验结果发现:甘油、山梨醇、乳酸与甲醇的混合添加均可以提高PGL的产量,其中山梨醇与甲醇的混合流加效果最为显著。研究表明,通过双碳源混合流加可以提高细胞活力,增强醇氧化酶活力,提高毕赤酵母表达外源蛋白效率。当山梨醇的流速为3.6g/(h·L)时,PGL酶活可达1593U/mL,生产强度为16.7U/(mL·h),比对照分别提高了84.6%和45.2%,实现了碱性果胶酶的高效生产。     

酶法测定甲醇酵母发酵液中甲醇浓度

用醇氧化酶－过氧化氢酶联合的酶促反应法,测定甲醇酵母发酵诱导阶段变化的发酵液中甲醇浓度,建立一种能够快速测定发酵液中甲醇浓度的方法,测定的最佳浓度范围是0．5－5％。     

产乙醇酸氧化酶的重组毕赤酵母的构建及催化合成乙醛酸的研究

乙醇酸氧化酶（Go）是植物光呼吸途径中的一种关键酶,可以催化乙醇酸生产乙醛酸。从新鲜菠菜叶中提取总RNA,利用RT-PCR技术获得编码GO基因的cDNA片断。通过基因重组将GO基因克隆到载体pA0815中,构建了胞内表达载体pA0815／GO,重组质粒经电转整合至甲醇营养酵母GS115染色体。在混合碳源为10g/L山梨醇和0．5g/L甲醇的培养条件下,细胞的GO酶活达到474IU／g（DCW）。利用该重组毕赤酵母作为催化剂生产乙醛酸,结果表明：在乙醇酸浓度为0．25mol／L,重组酵母湿菌体为10dL,黄素单核苷酸（FMN）浓度为0．01mmol／L,pH8．0,20℃,反应18h后乙醛酸的产率达到51．8％。     

毕赤酵母基因工程菌胞内AOX酶的检测方法

巴斯德毕赤酵母(Pichia pastoris)作为外源基因的表达宿主,已成功表达出一系列胞内和胞外蛋白[1～6],并已建立起了一套较成熟的发酵工艺.巴斯德毕赤酵母基因工程菌的外源基因,由胞内AOX酶(乙醇氧化酶)基因启动子调控.在非甲醇碳源条件下(如甘油或葡萄糖),AOX酶基因表达被抑制,外源基因也处于不表达状态.而以甲醇为唯一碳源时,AOX酶在胞内大量合成,同时外源基因被调控表达.在一般情况下,AOX酶的变化直接反映了外源基因的表达状况,因此通过分析检测胞内AOX酶的含量和变化速率,就可以确定外源基因所处的状态.     

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.     

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。     

海参i-型溶菌酶在毕赤酵母基因工程菌中优化表达及纯化

将实验室已构建的毕赤酵母基因工程茵(pPIC9K-SjLys/GS115)作为海参i-型溶茵酶生产菌株,本研究分别从甲醇浓度、培养基pH、温度和诱导时间对其产酶发酵条件进行优化.实验得出甲醇诱导浓度为1.0％,发酵培养基初始pH 6.0,温度30℃,培养96 h为最佳目的蛋白表达条件,其发酵液中海参i-型溶菌酶含量达10.63 mg/L.将发酵液经离心和超滤浓缩后得到上清液,再经离子交换和凝胶过滤层析纯化获得海参i-型溶菌酶产品,其酶活力达826.44 U/mg.经测定该酶对革兰氏阳性菌溶壁微球菌和革兰氏阴性菌副溶血弧菌均具有明显的抑菌作用.     

Metabolic flux analysis for recombinant protein production by Pichia pastoris using dual carbon sources: Effects of methanol feeding rate

The intracellular metabolic fluxes through the central carbon pathways in the bioprocess for recombinant human erythropoietin (rHuEPO) production by Pichia pastoris (Mut⁺) were calculated to investigate the metabolic effects of dual carbon sources (methanol/sorbitol) and the methanol feed rate, and to obtain a deeper understanding of the regulatory circuitry of P. pastoris, using the established stoichiometry‐based model containing 102 metabolites and 141 reaction fluxes. Four fed‐batch operations with (MS‐) and without (M‐) sorbitol were performed at three different constant specific growth rates (h^?1), and denoted as M‐0.03, MS‐0.02, MS‐0.03, and MS‐0.04. Considering the methanol consumption pathway, the M‐0.03 and MS‐0.02 conditions produced similar effects and had >85% of formaldehyde flux towards the assimilatory pathway. In contrast, the use of the dual carbon source condition generated a shift in metabolism towards the dissimilatory pathway that corresponded to the shift in dilution rate from MS‐0.03 to MS‐0.04, indicating that the methanol feed exceeded the metabolic requirements at the higher µ₀. Comparing M‐0.03 and MS‐0.03 conditions, which had the same methanol feeding rates, sorbitol addition increased the rHuEPO synthetic flux 4.4‐fold. The glycolysis, gluconeogenesis, and PPP pathways worked uninterruptedly only at MS‐0.02 condition. PPP and TCA cycles worked with the highest disturbances at MS‐0.04 condition, which shows the stress of increased feeding rates of methanol on cell metabolism. Biotechnol. Bioeng. 2010; 105: 317–329. © 2009 Wiley Periodicals, Inc.     

重组毕赤酵母产木聚糖酶的发酵条件优化研究

采用单因素实验确定重组毕赤酵母产木聚糖酶生长相的最适条件,然后利用Plackett—Bur—man实验设计对诱导相培养基成分和培养条件的10个因素进行筛选,方差分析结果表明,影响木聚糖酶表达的主要因子为酵母膏、诱导pH和摇床转速;在此基础上,用Box—Behnken的响应面方法对3个因素进行进一步优化,当酵母膏为11．13彰L,pH为6．38,摇床转速为228r／min时酶活有最大值,为262．77u／mL,较优化前提高了175．44％。优化后的摇瓶发酵条件应用于7L发酵罐并连续诱导培养120h,发现诱导72h后的木聚糖酶酶活最高,为2054．89u／mL。     

Production process for recombinant human angiostatin in Pichia pastoris

A pilot-scale production method of recombinant human angiostatin, a 38-kD fragment of plasminogen which has been reported to have antiangiogenic activity, has been successfully established by expressing the protein in the methylotrophic yeast Pichia pastoris. The secreted protein inhibited cultured endothelial cell proliferation in vitro and Lewis lung carcinoma growth in mice. The fermentation process was carried out using an on-line methanol controller, administering methanol to the growing culture and keeping its concentration under 2 g L⁻¹. The fermentation lasted 90 h, of which 70 h were growth on methanol. During growth on methanol the culture volume increased 64%, from 7 L to 11.5 L, producing 200 mg angiostatin and 5 kg of biomass. Journal of Industrial Microbiology & Biotechnology (2000) 24, 31–35. Received 12 May 1999/ Accepted in revised form 06 September 1999     

Heterologous expression,purification, and functional characterization of recombinant ovine angiotensinogen in the methylotrophic yeast Pichia pastoris

Angiotensinogen (AGT), a glycosylated plasma noninhibitory serpin, serves as a precursor for angiotensin peptides which regulate blood pressure and electrolyte balance. AGT is specifically cleaved by renin to produce angiotensin-I, the first product of the angiotensin-processing cascade. Ovine angiotensinogen (oAGT) is considered an effective substrate for human renin and consequently finds application in clinical renin assays. In this study, oAGT was cloned into the genome of Pichia pastoris and expressed under the control of alcohol oxidase (AOX1) promoter for high-level production. Compared to the shake flask study, the high cell density cultivation in bioreactor resulted in multifold increase in oAGT titer (420 ± 9.26 mg/L), which is its highest reported titer to date. We purified recombinant oAGT to homogeneity using two chromatography steps. The characterization studies revealed oAGT underwent a two-state transition during thermal denaturation process as assessed by differential scanning fluorimetry, and the melting temperature (T_m) of the purified oAGT from P. pastoris was 48.3°C. Renin reactivity with recombinant oAGT from P. pastoris (0.51 nM angiotensin-I/min) was slightly lower than the renin reactivity for recombinant oAGT from Escherichia coli (0.67 nM angiotensin-I/min), possibly because of its mannosylated N-glycan content. Enhanced production of functionally active recombinant oAGT using P. pastoris expression system reported in this study envisage the effective utilization of oAGT in clinical studies related to renin in near future.     

响应面分析优化产木聚糖酶毕赤酵母基因工程菌培养条件

研究不同碳源、氮源和无机盐对毕赤酵母AX181菌株产木聚糖酶的影响。实验表明,分别采用葡萄糖和玉米浆干粉为碳源和氮源可以明显提高木聚糖酶的产量。无机盐单因子优化实验显示添加适量的（NH4）2SO4、KH2PO4、MnSO4·H2O、FeSO4·7H2O也可以部分提高木聚糖酶产量。在此基础上利用响应面法优化毕赤酵母产木聚糖酶培养基,利用12次实验的Plackett—Burman设计实验筛选出影响产木聚糖酶的3个主要因素,即玉米浆干粉、MnSO4·H2O和FeSO4·7H20。并进一步通过最陡爬坡路径逼近最大响应区域,采用中心组合实验设计确定最佳条件。优化后的产木聚糖酶培养基组分为（g/L）：葡萄糖40．00,玉米浆干粉80．84,（NH4）2SO46．25,KH2PO41．25、MnSO4·H2O0．35,FeS04-7H2O1．31。培养基优化后,实际产酶2883．86u／mL,是优化前YPD培养基产酶的2．51倍。     

采用混合策略提高葡萄糖氧化酶在毕赤酵母中的表达水平

为了提高葡萄糖氧化酶 (GOD) 在毕赤酵母中的表达水平,提出了甲醇/山梨醇混合碳源诱导和共表达分子伴侣二硫键异构酶 (PDI) 和透明颤菌血红蛋白 (VHb) 两种策略。利用对照菌株X33/pPIC9k–GOD 在5 L发酵罐放大培养时,采用甲醇/山梨醇混合碳源诱导,GOD最终酶活为456 U/mL,比只采用甲醇作为单一碳源诱导时GOD最终酶活提高了20%。利用整合伴侣蛋白菌株X33/pPIC9k-GOD/pPICZ-PDI-VHb在5 L发酵罐进行高密度发酵,采用甲醇/山梨醇混合碳源诱导,GOD最终酶活达到716 U/mL,蛋白浓度为7.4 g/L。研究结果对提高外源蛋白在毕赤酵母中的表达有重要参考价值。     

Hypoxic fed-batch cultivation of Pichia pastoris increases specific and volumetric productivity of recombinant proteins

High cell density cultivation of Pichia pastoris has to cope with several technical limitations, most importantly the transfer of oxygen. By applying hypoxic conditions to chemostat cultivations of P. pastoris expressing an antibody Fab fragment under the GAP promoter, a 2.5-fold increase of the specific productivity q(P) at low oxygen supply was observed. At the same time the biomass decreased and ethanol was produced, indicating a shift from oxidative to oxidofermentative conditions. Based on these results we designed a feedback control for enhanced productivity in fed batch processes, where the concentration of ethanol in the culture was kept constant at approximately 1.0% (vv(-1)) by a regulated addition of feed medium. This strategy was tested successfully with three different protein producing strains, leading to a three- to sixfold increase of the q(P) and threefold reduced fed batch times. Taken together the volumetric productivity Q(P) increased 2.3-fold.     

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。     

巴斯德毕赤酵母表达外源蛋白的优化策略

巴斯德毕赤酵母(Pichia pastoris)表达系统已成为外源蛋白最理想的表达系统之一,诸多的优点体现了其广泛的研究价值和应用价值。综述了P.pastoris表达外源蛋白时在载体选择与利用、外源基因改造、翻译后修饰及表达稳定性等方面的优化策略,以加速其应用。     

Pichia pastoris: A highly successful expression system for optimal synthesis of heterologous proteins

One of the most important branches of genetic engineering is the expression of recombinant proteins using biological expression systems. Nowadays, different expression systems are used for the production of recombinant proteins including bacteria, yeasts, molds, mammals, plants, and insects. Yeast expression systems such as Saccharomyces cerevisiae (S. cerevisiae) and Pichia pastoris (P. pastoris) are more popular. P. pastoris expression system is one of the most popular and standard tools for the production of recombinant protein in molecular biology. Overall, the benefits of protein production by P. pastoris system include appropriate folding (in the endoplasmic reticulum) and secretion (by Kex2 as signal peptidase) of recombinant proteins to the external environment of the cell. Moreover, in the P. pastoris expression system due to its limited production of endogenous secretory proteins, the purification of recombinant protein is easy. It is also considered a unique host for the expression of subunit vaccines which could significantly affect the growing market of medical biotechnology. Although P. pastoris expression systems are impressive and easy to use with well-defined process protocols, some degree of process optimization is required to achieve maximum production of the target proteins. Methanol and sorbitol concentration, Mut forms, temperature and incubation time have to be adjusted to obtain optimal conditions, which might vary among different strains and externally expressed protein. Eventually, optimal conditions for the production of a recombinant protein in P. pastoris expression system differ according to the target protein.     

Genotyping of recombinant Pichia pastoris strains

A simplified amplified-fragment length polymorphism (AFLP) method was used to genotype Pichia pastoris strains obtained by transformation of P. pastoris strain GS115 with a single integration vector. A total of 14 transformants and 3 control strains were analyzed, which generated 16 different band patterns. A clonal variation was obtained after the transformation process due to genetic differences generated during the transformation event of the host strain. Furthermore, the cluster analysis showed that the transformants with lesser genetic differences with respect to the P. pastoris host strain are the recombinant strains with the highest level of recombinant protein production.     

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.