重组大肠杆菌生产谷胱甘肽发酵条件的研究

研究了重组Ｅ．Ｃｏｌｉ产ＧＳＨ的发酵条件,重点考察了添加酵母膏、前体氨基酸和ＡＴＰ的影响。结果发现,前体氨基酸和ＡＴＰ均能促进胞内ＧＳＨ的积累,若在发酵０ｈ和１２ｈ分别加入２０ｇ／ＬＡＴＰ和９ｍｍｏｌ／Ｌ前体氨基酸,则细胞干重和胞内ＧＳＨ含量可分别比对照提高２４％和１４倍。应用正交试验得出的针对细胞干重和ＧＳＨ总量的最佳组合,最大细胞干重和ＧＳＨ总量比原试验中的最好结果分别提高了１０％和２６％。在分析了该菌对葡萄糖利用情况的基础上,对该菌进行了指数流加培养,２５ｈ细胞干重与发酵液内ＧＳＨ总量分别达到８０ｇ／Ｌ和８８０ｍｇ／Ｌ,比摇瓶最好结果分别提高了８３和４６倍。     

活性干酵母SOD摇瓶发酵条件的研究

研究了营养与环境条件对耐高温酒精活性干酵母（ＴＨ－ＡＡＤＹ）ＳＯＤ摇瓶发酵的影响。实验结果表明,初糖浓度,金属离子、ＰＨ值、通气量（装液量）和培养时间等均对ＡＡＤＹ摇瓶发酵的生物量和ＳＯＤ含量有较大的影响。在实步优化的发酵条件下,细胞生物量为３９．６ｇ／Ｌ,菌体ＳＯＤ含量为１９４８Ｕ／ｇ,发酵液产酶能力为７．７万Ｕ／Ｌ。     

重组大肠杆菌的高密度发酵和甘油生产条件的初步研究

在摇瓶中进行重组大肠杆菌菌株BL21高密度发酵条件的研究,考察了葡萄糖浓度、盐离子浓度、温度、接种量、发酵时间等对该菌株生产甘油的影响。初步确定底物浓度为2.5%,盐离子浓度0.2%,温度为37℃,接种量为2%,经24h的摇瓶发酵,甘油产量最高达6.8g/L。在30L发酵罐实验中、按初步确定的优化条件发酵26h,甘油产量可达46.67g/L,是LB/葡萄糖培养基中甘油产量的2.06倍。     

重组大肠杆菌高密度发酵生产RGD-TRAIL的条件优化

本文以一株产RGD-TRAIL的重组大肠杆菌为研究对象,在10L发酵罐中考查了诱导温度、pH值、溶氧、流加葡萄糖对重组大肠杆菌生长和RGD-TRAIL蛋白表达的影响。结果表明:诱导温度25℃,pH值控制7.0,溶氧控制30%,以5g·L~(-1)·h~(-1)流速流加葡萄糖最有利于菌体生长和蛋白表达,菌体收率和RGD-TRAIL产量分别达到45.99g·L~(-1)和160.2mg·L~(-1)。     

类球红细菌SOD发酵条件优化

本文对类球红细菌3757产SOD进行了发酵条件优化,结果得到了较优的培养基组成(g/L):苹果酸3,胰蛋白胨4,磷酸氢二钾0.9,磷酸二氢钾O.6,硫酸镁0.2,无水氯化钙0.075,硫酸亚铁0.012,EDATA 0.02,微量元素溶液10 mL,生长因子溶液10 mL,pH 7.5。其中,微量元素溶液配方(g/L):硼酸2.8,硫酸锰1.6,钼酸钠0.76,硫酸锌0.24,硫酸铜0.04;生长因子溶液配方(g/L):维生素B_1 1,烟酰胺(VPP)1,生物素0.016,对氨基苯甲酸1。较优培养条件为:接种量5%,转速150 r/min,种龄24 h,发酵温度32℃,发酵时间24 h。优化后酶活力较优化前提高了88.0%。     

大肠杆菌发酵生产L-色氨酸工艺简析

本文对L-色氨酸进行了简要概述,指出利用大肠杆菌工程菌直接发酵生产L-色氨酸为国内主流方法,并对其成熟的发酵工艺控制、提取工艺进行了简析,并指出部分可进一步优化的工艺点。其中发酵工艺简析包括菌种培养基增加一定溶度抗生素和控制发酵温度来控制质粒稳定性;分析物料作用并提出优化后的种子、发酵培养基组成;菌种无需控制溶氧,而发酵则用溶氧反馈补料;控制乙酸和氨氮浓度、顺序升温缩短周期降低抑制性副产物作用。分离提取工艺简析包括硫酸酸化p H2-3,陶瓷膜过滤并控制滤液平均单位为14000-18000u/ml,阳离子树脂纯化,醋酸调p H5.89,0.5%活性炭60℃脱色20-30min,蒸发浓缩结晶,纯化水洗涤整条工艺路线。     

用重组大肠杆菌发酵生产人生长激素研究

通过不同培养基、不同糖浓度对重组菌Ｅ．ｃｏｌｉＤＨ１０Ｂ／ｐＩＮⅢＡ３ＨＧＨ的菌体生长与外源蛋白表达量的影响的比较，确定较为合适的培养条件，并对发酵过程中调节ｐＨ的氨水用量与外源蛋白的表达量之间的相关性作探索，得到相关性曲线，从而根据氨水用量了解细菌的生长状况。     

重组大肠杆菌高密度发酵生产类人胶原蛋白Ⅱ条件优化

通过考察pH、培养温度、溶解氧浓度和诱导时机对细胞生长和类人胶原蛋白Ⅱ表达的影响, 确定这些因素的最佳控制范围, 优化发酵条件。结果表明: 控制初始pH为6.5, 诱导后pH为6.8, 培养温度34°C, DO 20%及在对数生长后期进行诱导, 有利于细胞生长和外源基因的表达, 最终细胞密度为88.4 g/L, 类人胶原蛋白Ⅱ产量达到14.2 g/L。     

基因重组大肠杆菌表达HrpNEcc蛋白的发酵条件及诱导条件优化

对已构建好的表达HrpNEcc蛋白的工程菌BL21(DE3)/pET30a(+)hrpN Ecc的摇瓶发酵条件及乳糖诱导进行优化, 通过在7L发酵罐中放大发酵实验,以期提高蛋白产量并降低生产成本。在摇瓶中优化的发酵及诱导条件是：5% 的接种量,TB培养基,菌体培养至对数生长前期,添加3g/L外源诱导剂乳糖时,HrpNEcc蛋白产量可达417.60mg/L,比不添加乳糖时提高了36.73%,比用IPTG诱导时提高了16.85%。7L发酵罐中发酵,获得菌体湿重达到57.24g/L（WCW）,可溶性HrpNEcc蛋白产量占细胞总蛋白的50.2%,为3.29 g/L。     

Effects of environmental conditions on xylose fermentation by recombinant Escherichia coli

In batch fermentations, optimal conversion of xylose to ethanol by recombinant Escherichia coli was obtained under the following conditions: 30 to 37 degrees C, pH 6.4 to 6.8, 0.1 to 0.2 M potassium phosphate buffer, and xylose concentrations of 8% or less. A yield of 39.2 g of ethanol per liter (4.9% ethanol by volume) was observed with 80 g of xylose per liter, equivalent to 96% of the maximum theoretical yield. Maximal volumetric productivity was 0.7 g of ethanol per liter per h in batch fermentations and 30 g of ethanol per liter per h in concentrated cell suspensions (analogous to cell recycling).     

Effects of environmental conditions on xylose fermentation by recombinant Escherichia coli.

In batch fermentations, optimal conversion of xylose to ethanol by recombinant Escherichia coli was obtained under the following conditions: 30 to 37 degrees C, pH 6.4 to 6.8, 0.1 to 0.2 M potassium phosphate buffer, and xylose concentrations of 8% or less. A yield of 39.2 g of ethanol per liter (4.9% ethanol by volume) was observed with 80 g of xylose per liter, equivalent to 96% of the maximum theoretical yield. Maximal volumetric productivity was 0.7 g of ethanol per liter per h in batch fermentations and 30 g of ethanol per liter per h in concentrated cell suspensions (analogous to cell recycling).     

L-tyrosine production by recombinant Escherichia coli: fermentation optimization and recovery

L-tyrosine (L-tyr) overproducing Escherichia coli strain derived from an L-phenylalanine (L-phe) overproducing strain is characterized in 10 L and 200 L scale fermentations. Deletion of the chromosomal region encoding for the pheA gene, chorismate mutase/prephenate dehydratase, its leader peptide (pheL) and its associated promoter resulted in significant increase in L-tyr production (Olson et al., 2007. Appl Microbiol Biotechnol 74(5):1031-1040). Further increase in titer was achieved by overexpressing tyrA, encoding chorismate mutase/prephenate dehydrogenase, from a strong non-native trc promoter (Olson et al., 2007. Appl Microbiol Biotechnol 74(5):1031-1040). Fermentation optimization studies include media component selection; glucose feed optimization, antifoam agent selection, and understanding fermentation parameters affecting foaming. Generational stability of the strain was evaluated along with rate, titer, and yield of tyrosine formation from glucose. L-tyr titer of 55 g/L in 48 h was demonstrated in 200 L batches, is the highest titer published till date. We have also evaluated two primary separations schemes to isolate and purify L-tyr from the fermentation broth. Physical separation of L-tyr crystals from biomass using a decanter type centrifuge, based on the density difference between the solids, is compared and contrasted with a strategy where L-tyr is first dissolved at pH 11.5 and then acid precipitated from clarified supernatants following removal of biomass using membrane filtration. L-tyr product purity of 98% with yields ranging from 90% to 95% is demonstrated.     

重组大肠杆菌生产L-色氨酸发酵条件优化

为了提高重组大肠杆菌FB讲／pSV－04发酵生产L－色氨酸的产量,减少代谢副产物乙酸的生成,考察了比生长速率和无机盐对重组大肠杆菌发酵生产L．色氨酸的影响。在确定了合适的比生长速率和无机盐浓度之后,乙酸积累很少,L-色氨酸的产量为53．4g／L,比优化前提高了141．6％。经30L发酵罐初步放大,L－色氨酸的产量达53．6g／L,发酵结果稳定,具有工业化应用前景。     

Expression of a thermostable restriction endonuclease in recombinant Escherichia coli cells and optimization of fermentation conditions

Taq I restriction endonuclease gene of the thermophilic eubacterium Thermus aquaticus YT-1 (ATCC 25104) was successfully cloned and expressed in recombinant Escherichia coli cells under the control of the lac promoter/operator system. Higher Taq I endonuclease specific activities and biomass yields were obtained from E. coli ER2508(pUCTaq) cells when they were induced at the late-exponential phase of their growth. Taq I endonuclease expression was found to be host strain-dependent such that, among the three different strains examined, E. coli XL1(pUCTaq) produced the highest specific Taq I endonuclease activities for longer induction periods. Decreasing the inducer concentration from 1 to 0.1 mM not only improved the specific enzyme activity yields but also is more economical, considering the high cost of isopropyl--D-thiogalactopyranoside (IPTG). The optimum culture temperature was found to be 37 °C. Taq I endonuclease specific activity recovered from E. coli XL1(pUCTaq) cells was 935 U/mg under optimum conditions.     

Rapid protein release from Escherichia coli by chemical permeabilization under fermentation conditions

Overall protein release greater than 75% in less than 1 h can be attained by exposing exponentially growing Escherichia coli cells to 0.4 M guanidine plus 0.5% Triton X-100 at 37 degrees C in medium. Cell growth stops immediately upon addition of the chemicals, but the cells are not lysed. Guanidine concentrations lower than 0.2 M, in conjunction with 0.5% Triton X-100, do not release significant intracellular protein, nor do they inhibit cell growth. Under these conditions, the cells undergo an adaptation that confers resistance to protein release by further treatment with guanidine and Triton X-100. Cells treated with 0.2 M guanidine plus 0.5% Triton X-100 display intermediate behavior. Protein release is approximately 35%, and growth is temporarily interrupted by an extended lag phase. Subsequent resumption of cell growth results in resistant cells and no additional protein release. This resistance is shown to be reversible and is most likely due to physiological adaptation rather than genetic mutation.     

Effects of culture conditions on yield of Shiga-like toxin-IIv from Escherichia coli

The effects of selected culture conditions on production of Shiga-like toxin-II variant by an edema disease strain of Escherichia coli (412) and E. coli TB1 (pCG6) containing the cloned genes for Shiga-like toxin-II variant were examined. Incubation time, culture media, incubation temperature, starting pH of the culture medium, aeration, static culture, anaerobiosis, carbon sources, amino acids, antibiotics, and mitomycin C were investigated. The study showed that Shiga-like toxin-II variant was primarily cell associated and that strain TB1 (pCG6) produced as much as 100 times more toxin than did strain 412. Culture conditions that resulted in the greatest yield of Shiga-like toxin-II variant were incubation at 37 degrees C for 24 h with shaking in syncase broth initially adjusted to pH 8.5. Aerobic culture with shaking resulted in higher yields of Shiga-like toxin-II variant than did static aerobic or anaerobic culture. Addition of various carbon sources or amino acids, or tetracycline, lincomycin, or trimethoprim:sulfadoxine did not increase yields of toxin. The amount of Shiga-like toxin-II variant in supernatant preparations from strain TB1 (pCG6) was significantly increased by addition of mitomycin C to the culture medium.     

Process optimization for increased yield of surface-expressed protein in Escherichia coli

The autotransporter family of Gram-negative protein exporters has been exploited for surface expression of recombinant passenger proteins. While the passenger in some cases was successfully translocated, a major problem has been low levels of full-length protein on the surface due to proteolysis following export over the cytoplasmic membrane. The aim of the present study was to increase the surface expression yield of the model protein SefA, a Salmonella enterica fimbrial subunit with potential for use in vaccine applications, by reducing this proteolysis through process design using Design of Experiments methodology. Cultivation temperature and pH, hypothesized to influence periplasmic protease activity, as well as inducer concentration were the parameters selected for optimization. Through modification of these parameters, the total surface expression yield of SefA was increased by 200 %. At the same time, the yield of full-length protein was increased by 300 %, indicating a 33 % reduction in proteolysis.