重组巴氏毕赤酵母高密度发酵表达rHSA

对基因工程菌Pichiapastoris的摇瓶发酵条件进行了试验 ,并根据摇瓶发酵的优化结果进行了补料分批高密度发酵。在摇瓶发酵时 ,甲醇诱导基因工程菌P .pastoris表达重组人血清白蛋白的发酵周期为 96h ;甲醇的最佳诱导浓度为 1 0g L ;发酵pH范围为 5 72～ 6 5 9;在摇瓶培养时 ,随着接种量的增加 ,虽然目的蛋白表达量缓慢增加 ,但单位细胞光密度的蛋白产率却明显下降 ,符合y =1 2 941x- 0 50 59方程 (线性相关系数r=0 9789) ,其限制性因子很可能为溶氧。在分批发酵 ,接种量为 1 0 %且种子细胞光密度 (OD60 0 )为 2 0左右时 ,细胞生长的延迟期为 2 1 1h左右 ,细胞生长光密度与培养时间的关系模型为 :y =0 7841e0 .2 3 19t(线性相关系数r=0 .993 6 ) ;在补料发酵时细胞干重浓度可达到 1 1 5g L— 1 6 0g L ,在 1 2 0h重组人血清白蛋白表达量最大达到 3 6g L。     

表达血管生长抑制素的重组毕赤酵母在诱导阶段混合碳源的流加

为进行高密度发酵并实现外源基因的高表达,在表型为Mut^S的重组毕赤酵母（Pichia pastoris）表达人血管生长抑制素的诱导阶段,采用了甘油甲醇混合补料的培养方式。以溶氧水平作为甘油代谢指针来控制甘油限制性流加既可维持一定菌体生长,又不会发生发酵液中残余甘油及有害代谢产物（乙醇）阻遏蛋白表达。当表达阶段的菌体平均比生长速率控制于0.012h^-1,菌体浓度达150 g/L,血管生长抑制素浓度最高达到108 mg/L,血管生长抑制素的平均比生产速率为0.02 mg/(g·h),菌体关于甘油的表观得率为0.69 g/g,菌体关于甲醇的表观得率为0.93g/g,较没有采用甘油限制性流加时都有所提高。     

甘油相控制策略对重组毕赤酵母表达瑞替普酶(reteplase)的影响

研究了甘油补料策略对毕赤酵母表达reteplase(rPA)的发酵过程中细胞的生长和rPA表达的影响。通过将对甘油补料速率由10g/L.h-1增大到20g/L.h-1,细胞比生长速率,甘油的比消耗速率,甘油得率等都得到极大提高。而且,诱导期细胞生长,甲醇消耗和rPA的生成速率都增加,rPA的最大表达量从140.2mg/L增加到199.5mg/L。此另外,甘油补料时间也是影响rPA表达的重要因素,甘油补料时间短,细胞密度小,表达rPA少,甘油补料时间长,细胞密度增大,rPA的表达速率也增加,但是到诱导后期,细胞死亡率增大,蛋白酶释放增加,rPA的降解增强。     

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)。     

金龟子绿僵菌IMI330189液体发酵动力学研究

研究了金龟子绿僵菌IMI330189的液体发酵动力学。利用Sigmoid函数构建了该菌株液体发酵过程中的菌体生长和底物消耗的动力学模型,并运用Origin7.5软件拟合求解出各模型参数。结果表明,模型能够较好地拟合绿僵菌IMI330189液体发酵过程,其比生长速率在发酵第22.8h达到最大值,为0.084h-1;总糖比消耗速率在第9.6h达到最大值,为0.246h-1;总氮比消耗速率在第10.3h达到最大值,为0.007h-1;菌体对总糖的得率系数在39.8h达到最高,为0.861g/g。模型拟合和实验数据具有良好的适应性,基本反映了绿僵菌IMI330189液体发酵过程的动力学特征,为其液体发酵工艺的优化和发展奠定了基础。     

费氏中华根瘤菌M6-3合成多聚羟基丁酸的发酵动力学研究

采用分批和连续培养的方法对中华根瘤菌M6 - 3合成多聚羟基丁酸的发酵动力学进行了研究 ,实验结果表明 ,该菌合成多聚羟基丁酸的发酵类型属于部分生长关联型。其细胞生长速率与限制性基质葡萄糖之间的关系符合Monod方程式。其合成PHB的速率公式为 :dpdt=0 0 76 2x - 0 2 192 dxdt,细胞的生长耗糖得率系数 (yG)为 1 4 1(g干细胞 g葡萄糖 ) ,细胞的维持耗糖系数 (m)为 0 0 34 (g葡萄糖 h·g细胞 ) ,产物得率耗糖系数 (yp)为 0 133(gP(3HB) g葡萄糖 ) ;并且通过实验与回归数理分析建立了一系列发酵动力学模型。     

螺旋藻连续培养与动力学模型

在内循环气升式光生物反应器中 ,研究了钝顶螺旋藻 (SpirulinaplatensisGeitler)细胞的连续生长及其对碳源底物的利用特性。结果表明 :随着稀释率的增大 ,反应器中碳源浓度和细胞浓度分别呈上升和下降趋势 ,它们之间的关系可用Monod类型的方程很好地加以关联。细胞产率和碳消耗速率与稀释率的关系存在峰值现象 :在本实验条件下 ,最大细胞产率为 0 .36 2g/(L·d) ,最大碳消耗速率为 0 .177g/(L·d) ,此时稀释率为 0 .45 /d ,细胞浓度为OD560 =1.2 82 ,细胞对碳的得率系数为 2 .0 5 0g/g。所提出的连续培养动力学模型与实验数据拟合较好     

共表达甘油脱氢酶和二羟丙酮激酶对大肠杆菌生长及甘油代谢的影响

考察共表达甘油脱氢酶(GldA)和二羟丙酮激酶(DhaKLM)对大肠杆菌生长及甘油代谢的影响。结果表明:在好氧条件下,共表达甘油脱氢酶及二羟丙酮激酶可以提高大肠杆菌利用甘油合成菌体的效率,利用等量的甘油,重组菌最高菌密度比对照菌提高了70%,细胞干质量为3.54 g(以每升发酵液计)。在厌氧条件下,仅共表达甘油脱氢酶并不能促进大肠杆菌的甘油代谢,而同时共表达甘油脱氢酶和二羟丙酮激酶可以明显提高大肠杆菌代谢甘油的能力,每克菌体消耗的甘油量提高了42%,每克干细胞中达11.08 g,代谢产物组成也发生显著变化,乙酸成为主要产物。这说明共表达gldA及dhaKLM基因能有效促进大肠杆菌好氧利用甘油生长及厌氧甘油代谢的能力。     

不同渗透压调节剂对Candida krusei生理代谢的影响*

比较了氯化钠、氯化钾、甘露醇存在的高渗环境下克鲁氏假丝酵母(Candida kru-sei)的生理代谢。3种渗透压调节剂对C.krusei生理代谢影响有显著差异。与甘露醇相比,氯化钠和氯化钾对细胞生长的影响更为显著,而氯化钾对细胞的毒性则又小于氯化钠。细胞对糖的消耗速率依次为甘露醇>氯化钾>氯化钠。甘油和海藻糖是C.krusei在高渗环境下的主要相容性溶质。氯化钠和氯化钾对甘油合成的促进作用明显高于甘露醇。在0.6mol/L氯化钠、氯化钾、甘露醇存在时,细胞甘油浓     

葡萄糖氧化酶产生菌Z—l—C的分批发酵与恒化培养

本文对葡萄糖氧化酶产生菌z—I—c的分批发酵与恒化培养进行了研究。实验发现,在以葡萄糖为生长限制性基质的恒化培养中,该产生菌的维持系数为O．04 g葡萄糖／g菌体．H,生长得率系数Y^max_G=O．714 g菌体／g葡萄糖,最大比生长速率μmax=O．385h^-1,饱和常数Ks=4．76g/L,理论最适稀释度Dm=0．260h^-1,最大酶比活(E／x)max为2．16×10³μ／mg,其值较分批发酵的最大酶比活(1．5l×10³μ／mg)提高43％。当向恒化培养的补料培养基中添加0．02％的α-甲基-D-葡萄糖时,由于该葡萄糖结构类似物的诱导作用,可使(E／x)max达3．11×10³μ／mg,较分批发酵之值提高106％。     

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%。     

High-level expression and stabilization of recombinant human chitinase produced in a continuous constitutive Pichia pastoris expression system

A continuous fermentation process has been developed in Pichia pastoris (P. pastoris) with the glyceraldehyde-3-phosphate dehydrogenase (GAP) promoter in order to produce large quantities of recombinant human chitinase (rh-chitinase) for preclinical studies as a potential high-dose antifungal drug. Expression levels of about 200 to 400 mg/L have been demonstrated in fed-batch fermentations using strains with either the traditional methanol-inducible or the constitutive GAP promoter. Proteolytic degradation of the enzyme was typically seen in fed-batch fermentations. Continuous production of the enzyme by P. pastoris with the GAP promoter was demonstrated in a 1.5-L working volume fermentor using either glucose or glycerol as the carbon source. The fermentation could be extended for >1 month with a steady-state protein concentration of approximately 300 mg/L. Cell densities were >400 g/L wet cell weight (WCW) (approximately 100 g/L dry cell weight [DCW]) at a dilution rate (D) of 0.83 day(-1) or 1.2 volume exchanges per day (VVD). No proteolytic degradation of the enzyme was seen in the continuous fermentation mode.     

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。     

碱性果胶酶在重组毕赤酵母中高效表达的关键因素研究

为提高重组毕赤酵母生产碱性果胶酶的产量和生产强度, 在摇瓶条件下优化了重组毕赤酵母生产碱性果胶酶的关键因素。结果表明, 以下条件：初始甘油浓度40 g/L、初始甲醇浓度3.1 g甲醇/g DCW、每24 h添加0.51 g甲醇/g DCW、诱导表达周期72 h、250 mL三角瓶诱导培养基装液量30 mL、初始pH 6.0, 最适于菌体生长与产物表达。在此基础上, 7 L罐上通过恒速流加甘油进一步提高细胞密度, 诱导阶段甲醇采取前期恒速流加和后期DO-stat, 发酵结束菌体干重达80 g/L, 酶活为217 U/mL, 比摇瓶结果提高了66.2%。     

碱性果胶酶在重组毕赤酵母中高效表达的关键因素研究

为提高重组毕赤酵母生产碱性果胶酶的产量和生产强度,在摇瓶条件下优化了重组毕赤酵母生产碱性果胶酶的关键因素。结果表明,以下条件：初始甘油浓度40g／L、初始甲醇浓度3.1g甲醇／gDCW、每24h添加0.51g甲醇／gDCW、诱导表达周期72h、250mL三角瓶诱导培养基装液量30mL、初始pH6,0,最适于菌体生长与产物表达。在此基础上,7L罐上通过恒速流加甘油进一步提高细胞密度,诱导阶段甲醇采取前期恒速流加和后期DO-stat,发酵结束菌体干重达80g／L,酶活为217U／mL,比摇瓶结果提高了66.2％。     

Optimization of chemically defined medium for recombinant Pichia pastoris for biomass production

A chemically defined medium was optimized for the maximum biomass production of recombinant Pichia pastoris in the fermentor cultures using glycerol as the sole carbon source. Optimization was done using the statistical methods for getting the optimal level of salts, trace metals and vitamins for the growth of recombinant P. pastoris. The response surface methodology was effective in optimizing nutritional requirements using the limited number of experiments. The optimum medium composition was found to be 20 g/L glycerol, 7.5 g/L (NH4)2SO4, 1 g/L MgSO4.7H2O, 8.5 g/L KH2PO4, 1.5 mL/L vitamin solution and 20 mL/L trace metal solution. Using the optimized medium 11.25 g DCW/L biomass was produced giving a yield coefficient of 0.55 g biomass/g of glycerol in a batch culture. Chemostat cultivation of recombinant P. pastoris was done in the optimized medium at different dilution rates to determine the kinetic parameters for growth on glycerol. Maximum specific growth rate of 0.23 h(-1) and Monod saturation constant of 0.178 g/L were determined by applying Monod model on the steady state data. Products of fermentation pathway, ethanol and acetate, were not detected by HPLC even at higher dilution rates. This supports the notion that P. pastoris cells grow on glycerol by a respiratory route and are therefore an efficient biomass and protein producers.     

Kinetic comparison of seven strains of 2,4-dichlorophenoxyacetic acid-degrading bacteria.

Seven strains of 2,4-dichlorophenoxyacetic acid-degrading bacteria, including Pseudomonas, Alcaligenes, and Bordetella spp., were compared on the basis of growth kinetics. Estimates of maximum growth rate (mu max, k1) and half-saturation growth constant (Ks, k3) were obtained by fitting substrate depletion curves to a four-parameter version of the integrated Monod equation. Estimates of Ks ranged from 2.2 micrograms/ml (10 microM) to 33.8 micrograms/ml (154 microM), and estimates of mu max ranged from 0.20 h-1 (Td = 3.5 h) to 0.32 h-1 (Td = 2.2 h). Estimates of mu max, but not Ks, were affected by changes in initial inoculum density. Maximum growth rates (mu max) were also estimated from turbidity measurements. They ranged from 0.10 h-1 (Td = 6.9 h) to 1.0 h-1 (Td = 0.7 h). There was no correlation between estimates of mu max derived from substrate depletion curves and those derived from turbidity measurements (P = 0.20).     

Kinetic comparison of seven strains of 2,4-dichlorophenoxyacetic acid-degrading bacteria.

Seven strains of 2,4-dichlorophenoxyacetic acid-degrading bacteria, including Pseudomonas, Alcaligenes, and Bordetella spp., were compared on the basis of growth kinetics. Estimates of maximum growth rate (mu max, k1) and half-saturation growth constant (Ks, k3) were obtained by fitting substrate depletion curves to a four-parameter version of the integrated Monod equation. Estimates of Ks ranged from 2.2 micrograms/ml (10 microM) to 33.8 micrograms/ml (154 microM), and estimates of mu max ranged from 0.20 h-1 (Td = 3.5 h) to 0.32 h-1 (Td = 2.2 h). Estimates of mu max, but not Ks, were affected by changes in initial inoculum density. Maximum growth rates (mu max) were also estimated from turbidity measurements. They ranged from 0.10 h-1 (Td = 6.9 h) to 1.0 h-1 (Td = 0.7 h). There was no correlation between estimates of mu max derived from substrate depletion curves and those derived from turbidity measurements (P = 0.20).     

High yield production of a mutant Nippostrongylus brasiliensis acetylcholinesterase in Pichia pastoris and its purification

The mutant M301A of the acetylcholinesterase B from Nippostrongylus brasiliensis (NbAChE) was produced in a high-cell-density fermentation of a recombinant methylotrophic yeast Pichia pastoris. Dissolved oxygen (DO) spikes were used as an indicator for feeding the carbon source. Wet cell weight (WCW) reached after 8 days a maximum value of 316 g/L and the OD600 at this time was 280. The acetylcholinesterase activity increased up to 6,600 U/mL corresponding to an expression rate of 2 g of NbAChE per liter supernatant. The specific activity of the mutant NbAChE was determined after purification as 3,300 U/mg. Active site titration with chlorpyrifos, a strong AChE inhibitor, yielded in a specific activity of 3,400 U/mg. The enzyme was secreted by Pichia pastoris. Therefore, it could be concentrated from culture broth by cross-flow-filtration (50 kDa cut-off membrane). It was further purified in one-step anion-exchange chromatography, using a XK 50/20 column filled with 125 mL Q Sepharose HP. Mutant NbAChE was purified 1.9-fold up to a purity of 97% and a yield of 87%. The isolated enzyme was nearly homogenous, as seen on the silver stained SDS-PAGE as well as by a single peak after gel filtration. This extraordinary high expression rate and the ease of purification is an important prerequisite for their practical application, for example in biosensors for the detection of neurotoxic insecticides.