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。     

利用不同碳源进行毕赤酵母高密度发酵及TEF-1启动子指导下的HPV16_L1蛋白表达

目的:研究不同碳源对于毕赤酵母菌株在发酵罐中高密度生长,以及对组成型翻译延伸因子-1(TEF-1)启动子指导下HPV16_L1蛋白表达的影响。方法:利用1.5L发酵罐使用不同碳源进行毕赤酵母的高密度发酵,检测在不同碳源利用情况下菌体的增殖动力学,并以Western blot动态分析HPV16_L1蛋白的表达水平。结果:以甘油作为碳源,菌体细胞湿重可达到510g/L(OD600为189.4),HPV16_L1的表达在72h之前保持高水平;在甲醇和葡萄糖中菌体细胞湿重都可达到220g/L左右(OD600分别为75.3和77.3),甲醇利用下HPV L1蛋白在144h后仍保持较高水平表达,葡萄糖中60h HPV L1表达开始显著下降;在山梨醇作为碳源情况下菌体未能在发酵罐中获得高密度生长;总体上,甘油作为碳源在72h左右可获得最高的目的蛋白收获总量。结论:为实现毕赤酵母高密度生长与异源基因在TEF-1启动子指导下高效表达,以及HPV L1蛋白的简易、有效制备提供了基础。     

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。     

深黄被孢霉利用不同碳源产油脂比较

本研究主要探讨深黄被孢霉M2菌株对生物质全糖的利用,考察其碳源同化能力、不同碳源下产脂情况以及对玉米皮渣的利用能力。研究结果表明,M2菌株能够利用葡萄糖、木糖、阿拉伯糖和甘露糖进行生长和油脂积累。M2菌株以6%糖浓度的玉米皮渣水解液为底物发酵培养,油脂微生物生物量达18.2g/L,干菌体油脂含量45.7%,单位体积发酵液油脂产量为8.3g/L。     

Candida glycerinogenes metabolic fermentation using different carbon sources

研究了不同碳源对Candida glycerinogenes的菌体生长、发酵液pH值及代谢产物的影响,结果发现以葡萄糖、果糖等单糖为碳源时菌体生长较快,最终生物量比以蔗糖、麦芽糖等二糖为碳源时高20％～30％;导致发酵前12 h发酵液pH值明显下降的主要因素是乳酸;与葡萄糖为碳源转化为甘油相比,果糖为碳源时更易累积乙醇;以蔗糖、麦芽糖为碳源时,用于转化生成甘油的碳源明显降低,碳源主要用于菌体自身生物合成及HMP途径,以蔗糖为碳源时,用于乳酸、丙酸及柠檬酸生物合成的碳源较麦芽糖明显提高,TCA途径代谢较为活跃.     

高糖和氮源对鼠李糖乳杆菌(Lactobacillus rhamnosus)L-乳酸发酵的影响

鼠李糖乳杆菌经实验室耐高糖高酸选育,能够在高糖浓度下高效高产L-乳酸。以酵母粉为氮源和生长因子,葡萄糖初始浓度分别为120 g/L和146 g/L,摇瓶培养120h,L-乳酸产量分别为104g/L和117.5g/L,L-乳酸得率分别为86.7%和80.5%。高葡萄糖浓度对菌的生长和乳酸发酵有一定的抑制。增加接种量,在高糖浓度发酵条件下,可以缩短发酵时间,但对增加乳酸产量效果不明显。乳酸浓度对鼠李糖乳杆菌生长和产酸有显著的影响。初始乳酸浓度到达70g/L以上时,鼠李糖乳杆菌基本不生长和产酸,葡萄糖消耗也被抑制。酵母粉是鼠李糖乳杆菌的优良氮源,使用其它被测试的氮源菌体生长和产酸都有一定程度的下降。用廉价的黄豆粉并补充微量维生素液,替代培养基中的酵母粉,可以使产酸浓度和碳源得率得以基本维持。     

重组人抗血栓蛋白在大肠杆菌中的自诱导表达及纯化

旨在优化重组人抗血栓蛋白(rHAP)工程菌的自诱导培养基,以提高菌体产量及可溶性的重组rHAP蛋白含量.选取蛋白胨、酵母提取物、甘油、葡萄糖为因素,各取4个水平,采用正交表L16(45)进行试验设计,时影响菌体生长和可溶性rHAP表达水平的乳糖浓度进行了优化.结果表明自诱导培养基碳氮源的最优配比:2％蛋白胨,1.5％酵母,0.5％甘油,0.03％葡萄糖,0.2％乳糖.此时表达菌密度OD600和可溶性rHAP目标蛋白表达量分别是未优化前的2.04倍和2.85倍.在20 L发酵表达时,rHAP工程菌OD600值高迭93,菌体温量为1 620 g/20L.利用Q-Sepharose和SP-Sepharose纯化,Western blotting结果表明表达蛋白为目的融合蛋白.     

添加TCA循环中间产物加速光滑球拟酵母积累丙酮酸

在维生素限制的条件下,研究了添加TCA循环中间产物对光滑球拟酵母多重维生素营养缺陷型菌株CCTCC M202019生长和积累丙酮酸的影响。该菌株能以TCA循环中间产物为唯一碳源进行生长,且在以葡萄糖、乙酸和TCA循环中间产物为复合碳源的平板上菌落数高于分别以葡萄糖和乙酸或TCA循环中间产物为唯一碳源时的菌落数。与其它TCA循环中间产物相比,草酰乙酸更能促进细胞的生长、提高丙酮酸产量和对葡萄糖的得率。草酰乙酸能够促进细胞生长,是因为T. glabrata CCTCC M202019菌株能够利用乙酸作为乙酰辅酶A供体。在含有100 g/L葡萄糖和6 g/L乙酸钠的培养基中再添加10 g/L草酰乙酸进行分批发酵实验,可使菌体浓度从11.8 g/L提高到 13.6 g/L,增长幅度为15%;丙酮酸对葡萄糖的得率(0.66 g/g)以及生产强度(1.19 g·L^{-1<、sup>·h-1<、sup>)分别高出6%和24%,使发酵结束时间提前8～12h。}     

毕赤嗜甲醇酵母工程菌高密度培养表达黑曲霉菊粉内切酶的研究

目的:对毕赤嗜甲醇酵母工程菌inu-26高密度培养表达黑曲霉菊粉内切酶的条件进行优化,找出最佳的外源蛋白表达条件。方法:在摇瓶优化培养的基础上进行发酵罐高密度培养,优化最佳产酶条件。结果:以葡萄糖为碳源、微量元素添加量100～200mL/L、甲醇浓度1g/L、pH6.0～7.0、诱导时间96h时酶的表达量最高;摇瓶模拟高密度培养表明影响酵母生长的最主要因素葡萄糖和硫酸铵的最佳浓度分别为20～45和11.5g/L;利用培养基F1进行高密度培养优于其他培养基,工程菌生长符合指数生长曲线,细胞生长延迟期为1.36h,比生长速率μ为0.4846h-1。结论:以葡萄糖为碳源,采用葡萄糖-甲醇混合诱导和100%甲醇单一诱导相结合,在菌体鲜重约为280g/L时连续诱导96h,菌体生长良好,不会出现自溶,且酶的表达量最高,为摇瓶培养的3倍多,酶活最高可达540 U/mL。     

氨离子浓度对重组毕赤酵母的生长和血管生长抑制素表达的影响

本研究采用流加补料培养方式培养重组巴斯德毕赤酵母（Pichia pastoris）,表达血管生长抑制素（Angiostatin）。整个培养过程分为甘油为碳源的生长阶段和以甲醇为碳源的诱导阶段。全过程用氨水调节pH时,诱导阶段菌体生长受到抑制,蛋白的最大表达量为9.08mg/L。进行不同氨离子浓度的摇瓶培养,证实在以甲醇为碳源时,氨离子浓度对菌体的生长有明显的影响。高密度培养中改用2mol/L的KOH溶液调节pH,诱导阶段菌体有缓慢的生长,蛋白最大表达量增为20mg/L。     

Poly(3-hydroxybutyrate) (PHB) synthesis by recombinant Escherichia coli harbouring Streptomyces aureofaciens PHB biosynthesis genes: effect of various carbon and nitrogen sources

Recombinant Escherichia coli (ATCC:PTA-1579) harbouring poly(3-hydroxybutyrate) (PHB) synthesising genes from Streptomyces aureofaciens NRRL 2209 accumulates PHB. Effects of different carbon and nitrogen sources on PHB accumulation by recombinant E. coli were studied. Among the carbon sources used glycerol, glucose, palm oil and ethanol supported PHB accumulation. No PHB accumulated in recombinant cells when sucrose or molasses were used as carbon source. Yeast extract, peptone, a combination of yeast extract and peptone, and corn steep liquor were used as nitrogen sources. The maximum PHB accumulation (60% of cell dry weight) was measured after 48 h of cell growth at 37 degrees C in a medium with glycerol as the sole carbon source, and yeast extract and peptone as nitrogen sources. Scanning electron microscopy of the PHB granules isolated from recombinant E. coli revealed these to be spherical in shape with a diameter ranging from 0.11 to 0.35 pm with the mean value of 0.23 +/- 0.06 pm.     

Optimizing the expression of a monoclonal antibody fragment under the transcriptional control of the Escherichia coli lac promoter

The expression of a monoclonal antibody Fab fragment in Escherichia coli strain RB791/pComb3, induced with either lactose or isopropyl-beta-D-thiogalactoside (IPTG), was compared to determine if lactose might provide an inexpensive alternative to induction with IPTG. Induction of Fab expression imposed a metabolic load on the recombinant cells, resulting in lower final cell yields compared to the non-induced controls. An IPTG concentration of 0.05 mM was sufficient to achieve maximal expression of soluble Fab protein when inducing in the early-, mid-, or late-log phases of batch cultures grown using either glucose or glycerol as a carbon source. The largest overall yield of Fab fragments when using 0.05 mM IPTG was achieved by increasing the final yield of cells through glycerol feeding following induction in late-log phase. Lactose was as effective as IPTG for inducing Fab expression in E. coli RB791/pComb3. The greatest overall level of Fab expression was found when cells grown on glycerol were induced with 2 g/L lactose in late-log phase. Since the cost of 0.05 mM of IPTG is significantly greater than the cost of 2 g/L lactose, lactose provides an inexpensive alternative to IPTG for inducing the expression of Fab fragments, and possibly other recombinant proteins, from the E. coli lac promoter.     

Metabolism of cyclic adenosine 3'',5''-monophosphate and induction of tryptophanase in Escherichia coli.

The relationship between cyclic adenosine 3',5'-monophosphate (cyclic AMP) metabolism and the induction of tryptophanase and beta-galactosidase was studied in several strains of Escherichia coli grown with succinate, acetate, glycerol, or glucose as the carbon source. No consistent relationship between the intracellular concentration of cyclic AMP in the several strains cultured and the various carbon sources was discerned. In E. coli K-12-1 the induction of tryptophanase was found to vary in the order: succinate greater than acetate greater than glycerol greater than glucose, and that of beta-galactosidase was found in the order: glycerol greater than acetate greater than succinate greater than glucose. Rate of accumulation of cyclic AMP in the culture filtrate was in the order: succinate greater than acetate greater than glycerol greater than glucose. The addition of glycerol to E. coli K-12-1 grown in acetate caused inhibition of tryptophanase and slight inhibition of accumulation of extracellular cyclic AMP. These same conditions caused beta-galactosidase induction to be stimulated. The addition of exogenous cyclic AMP to cultures grown with four different carbon sources had an effect characteristic for each of the two enzymes studied as well as each individual carbon source. The results suggest that there are control elements distinct from cyclic AMP and its receptor protein which respond to the catabolic situation of the cell.     

Process development for production of recombinant human insulin-like growth factor-I in Escherichia coli

Fed-batch cultures were carried out to overproduce human insulin-like growth factor I (IGF-I) in Escherichia coli. The effects of carbon sources (glucose or glycerol) and induction time on cell growth and IGF-I production were investigated in more detail. Glycerol was a better carbon source than glucose for IGF-I production in fed-batch culture. Induction at the mid-exponential phase with glycerol as a carbon source in the pH-stat fed-batch culture was optimal for IGF-I production. Under this condition, 2.8 g L⁻¹ of fusion IGF-I was produced as inclusion bodies. We have also developed downstream processing for preparative scale purification of IGF-I from the fusion protein produced by the fed-batch culture using glycerol as a carbon source. After the fusion protein expressed was solubilized in 8 M urea and cleaved with hydroxylamine, the released IGF-I was purified by cation exchange chromatography, refolding and preparative scale reverse phase HPLC (rp-HPLC) to give recombinant IGF-I of >98% purity. The biological activities of the purified IGF-I were measured and found to be identical to those of commercial IGF-I. Journal of Industrial Microbiology & Biotechnology (2000) 24, 94–99. Received 13 January 1999/ Accepted in revised form 02 October 1999     

产HSA—CP融合蛋白毕赤酵母的发酵条件优化

为提高重组毕赤酵母生产人血清白蛋白-C肽融合蛋白（HSA—CP）的产量和生产强度,在摇瓶条件下考察了甲醇诱导时间和浓度对目的蛋白产量的影响。结果表明,质量浓度10g/L的甲醇诱导72h最适于产物表达。通过对7L发酵罐中各因素的优化,得到最佳条件为：初始甘油质量浓度10g/L,30℃培养,菌体生长期和诱导期的pH及溶氧分别控制在pH5．0、30％溶解O2或pH6．0、15％的溶解O2。10g/L的甲醇诱导72h,最终使干细胞质量浓度达到56．43g/L,目的蛋白产量达368．45mg／L。生产强度为3．920mg/（L·h）,目标蛋白的比生产速率为5．12mg/（L·h）。     

Linear correlation between online capacitance and offline biomass measurement up to high cell densities in Escherichia coli fermentations in a pilot-scale pressurized bioreactor

To yield high concentrations of protein expressed by genetically modified Escherichia coli, it is important that the bacterial strains are cultivated to high cell density in industrial bioprocesses. Since the expressed target protein is mostly accumulated inside the E. coli cells, the cellular product formation can be directly correlated to the bacterial biomass concentration. The typical way to determine this concentration is to sample offline. Such manual sampling, however, wastes time and is not efficient for acquiring direct feedback to control a fedbatch fermentation. An E. coli K12-derived strain was cultivated to high cell density in a pressurized stirred bioreactor on a pilot scale, by detecting biomass concentration online using a capacitance probe. This E. coli strain was grown in pure minimal medium using two carbon sources (glucose and glycerol). By applying exponential feeding profiles corresponding to a constant specific growth rate, the E. coli culture grew under carbon-limited conditions to minimize overflow metabolites. A high linearity was found between capacitance and biomass concentration, whereby up to 85 g/L dry cell weight was measured. To validate the viability of the culture, the oxygen transfer rate (OTR) was determined online, yielding maximum values of 0.69 mol/l/h and 0.98 mol/l/h by using glucose and glycerol as carbon sources, respectively. Consequently, online monitoring of biomass using a capacitance probe provides direct and fast information about the viable E. coli biomass generated under aerobic fermentation conditions at elevated headspace pressures.     

乳糖诱导的重组人血管内皮抑素(rhEndostatin)蛋白的表达

研究用乳糖替代IPTG作为诱导剂进行重组蛋白的表达,观察乳糖对乳糖操纵子调控的基因工程菌发酵及重组血管内皮抑素表达的影响,从而选取最佳诱导表达条件。以重组人血管内皮抑素表达工程菌pETrhEN/BL21(DE3)作为研究对象,分别用IPTG和乳糖作为诱导剂,在摇瓶中进行表达实验。并对重组蛋白质表达量进行分析。然后在5 L发酵罐中进行验证。在摇瓶培养条件下,乳糖浓度大于0.5 g/L即可以诱导目的蛋白的表达。乳糖浓度1 g/L时诱导目的蛋白表达量与1 mmol/L的IPTG相当,当乳糖浓度为10 g/L,目的蛋白表达量达到最大。在发酵罐培养条件下,补料4 h后葡萄糖浓度基本耗尽,此时开始加入乳糖。诱导后1 h,即有重组蛋白表达,在诱导后4 h达到高峰(占菌体可溶性蛋白的56%),与此同时,诱导后5 h菌体浓度也达到最高值。在以乳糖操纵子为调控手段的工程菌表达系统中,可以使用乳糖作为诱导剂,诱导应在葡萄糖消耗完后进行。     

Over-production of Thermus protease in dense culture of Escherichia coli using two carbon sources

Escherichia coli JM109(DE3) harboring expression plasmid pkAQNÆC30, which carries the Thermus protease aqualysin I (AQI) gene, was cultivated with glucose as a sole carbon source. The final cell concentration was over 15 g dry weight/l and the amount of AQI produced reached approximately 130 kU/ml broth. Moreover, by using two carbon sources, glucose and glycerol, the production yield was increased to over 200 kU AQI/ml, while suppressing the formation of inhibitory acetic acid.     

产酸丙酸杆菌生长特性及5L罐发酵动力学研究

论文在摇瓶水平对产酸丙酸杆菌基本生长特性（温度、pH、摇床转速、接种量、种龄等）、碳源、氮源利用情况、产物抑制及5 L罐发酵动力学进行了研究。结果表明,该菌在32℃,初始pH 6．5,摇床转速150 r/min,接种24 h的种子液,接种量为5％条件下,产酸丙酸杆菌生长及产酸水平达最高值;该菌可利用碳源十分广泛,但对氮源要求比较高,只可利用有机氮源;在不同初始葡萄糖浓度下,产酸丙酸杆菌生长及产酸水平差异不大,无明显底物抑制现象;在2g/L的初始丙酸盐浓度下,该菌生长受到明显抑制;在5L发酵罐中,初始葡萄糖浓度为58．8 g/L,发酵72 h,葡萄糖消耗完全,丙酸终浓度达22．4 g/L,丙酸得率和产率分别达0．381 g/g和0．295 g/（L·h）,丙酸占总酸比例达72．10％。     

Improved production of rifamycin SV by <Emphasis Type="Italic">Amycolatopsis mediterranei</Emphasis> MM2 by the feeding method of carbon source

The purpose of this research was to study the enhancement of rifamycin SV (RSV) yield according to the feeding method of a carbon source for Amycolatopsis mediterranei MM2. RSV produced during fermentation dropped sharply after reaching a maximum, and it was found that this trend of RSV production resulted from simultaneous production and degradation of RSV. To reduce RSV degradation during incubation, the effect of carbon source on cell growth was investigated. Based on the results, glucose was a better carbon source than glycerol for cell growth, although glycerol was better than glucose for RSV production, as reported in our previous study. To confirm this, RSV yield and dry cell weight (DCW) were measured according to the feeding method of carbon source using a 5-L size bioreactor. Results showed that initial cell growth rate and RSV yield were significantly increased regardless of the addition method of glucose into glycerol, provided glucose was present in the initial stage of cell growth.