用重组大肠杆菌JM109(pKST11)转化苯生产顺-1,2-二羟基-3,5-环己二烯

顺-1,2-二羟基-3,5-环己二烯（简称DHCD）是航天业、电子工业、医药业以及精细化工业上重要的手性化合物。利用重组E. coli JM109 (pKST11),采用适时监测发酵过程中全细胞甲苯双加氧酶（Toluene dioxygenase,TDO）活性的方法,研究了发酵生产DHCD工艺中的重要影响因子IPTG以及底物苯的供给方式对DHCD产量的影响。研究结果表明：（1）发酵初期利用IPTG诱导TDO的表达,不利于细胞生长,在对数生长中期（6或8h）,采用0.5mmol/L IPTG即可诱导出TDO的最高表达。（2）发酵液中的苯对全细胞甲苯双加氧酶(TDO)的活性有抑制作用,而利用液体石蜡作为缓释剂进行两相法发酵则降低了苯的毒害,明显提高了DHCD的产量。当采用传统的通气供苯方法,DHCD的产量仅有75 g/L;批式添加液体石蜡与苯的混溶物使DHCD的产量提高到226 g/L,是通气供苯法的3倍;而采用流加的方式添加液体石蜡与苯的混溶物使DHCD的产量进一步提高到368 g/L,是通气供苯法的5倍。证明通过发酵工艺的优化可以解决苯的毒害与苯作为反应底物在水相中需要有一定浓度之间的矛盾,获得较好的转化结果。     

生物转化合成苯乳酸工程菌的培养条件优化

本研究旨在优化重组大肠杆菌Escherichia coli BL21 (DE3) harboring pRSF-aad-ldh10-fdh菌株的培养条件,获得高密的供生物转化苯丙氨酸为苯乳酸的细胞。实验考察了摇瓶发酵培养基碳源、氮源种类和浓度,3 L发酵罐中转速和通气量及恒速补料、DO-stat和pH-stat等不同分批补料策略对菌体密度的影响。结果表明,当碳源为4 g/L葡萄糖,氮源为24 g/L安琪酵母浸粉FM802,细胞干重最大可达9.24 g/L;当转速为400 r/min和通气量为1.5 vvm时,细胞干重最大可达10.18 g/L;以4 g/(L·h)恒速流加葡萄糖时,细胞干重最大可达13.71 g/L。本研究还对工程菌酶表达的诱导条件进行了优化,菌体培养2 h后,添加终浓度为0.08 mmol/L IPTG诱导剂,在25℃下诱导培养14 h所得细胞有利于生物转化。底物苯丙氨酸浓度为60 g/L,转化为苯丙酮酸的转化率为50.2%,转化为苯乳酸的转化率为35.2%。     

外源物质对灵芝多糖和β-葡聚糖发酵的影响

研究了14种外源物质（化合物）对灵芝细胞生长和发酵合成多糖和β-葡聚糖的影响。结果表明,连翘水提物（3g/L）对灵芝细胞生长具有显著促进作用;薏苡仁酯（3g/L）对灵芝胞内多糖和β-葡聚糖的合成均具有促进作用;而桔梗水提物、硝酸铈铵、硝酸镨、茉莉酸甲酯和硝普钠对灵芝细胞生长和产物合成均具有抑制作用。进一步通过Box-Behnken试验设计和响应面法分析,建立了添加薏苡仁酯发酵产β-葡聚糖的二次多项式模型,经分析得到产β-葡聚糖的最优条件为：薏苡仁酯添加量10.5g/L、接种量16%、添加时间第88小时、发酵初始pH 7.00。在此条件下获得β-葡聚糖的产量可达(40.67±8.43)mg/L,与未添加薏苡仁酯的对照组相比,提高了41.86%;多糖产量为(0.99±0.21)g/L,与对照组相比,提高了31.99%。结果提示所得添加薏苡仁酯的优化条件可定向诱导灵芝β-葡聚糖的合成,同时也表明在灵芝液体发酵体系中添加薏苡仁酯发酵产多糖和β-葡聚糖具有一定的实用价值。     

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。     

控氧发酵对干酪乳杆菌合成苯乳酸的影响

在静置、搅拌及通气搅拌3种不同控氧条件下,分别用干酪乳杆菌Lactobacillus casei B3发酵及全细胞转化合成了苯乳酸,考察菌体生长、葡萄糖消耗及其发酵与转化合成苯乳酸的规律。结果表明:在转速100 r/min的搅拌条件下,L.casei B3发酵合成苯乳酸的浓度比静置发酵条件下提高了41.4%;但在空气流量2 L/min及转速100r/min的通气搅拌下,发酵合成苯乳酸的浓度较静置发酵时下降了60.3%;以8 g/L苯丙酮酸为底物,以相应静置、搅拌及通气搅拌条件下所得的菌体为全细胞催化剂转化合成苯乳酸,其摩尔转化率分别为67.2%、62.7%和35.9%。此结果说明:适度的搅拌促进了发酵过程的底物和产物传质,但充足或过量供氧会影响细胞内的转化合成酶系,不利于苯乳酸的全细胞转化合成。     

重组青霉素G酰化酶拆分制备（S）-邻氯苯甘氨酸

对产青霉素G酰化酶的重组枯草芽胞杆菌发酵产酶条件进行优化,确定优化后的发酵条件：可溶性淀粉10g/L、蛋白胨12g/L、酵母粉3g/L、NaCl10g,／L;pH7．5、培养温度37℃、装液量80mL（500mL三角瓶）、培养28h,青霉素G酰化酶的表达水平由最初的7．34U／mL提高至18．23U／mL。以表达青霉素G酰化酶的枯草芽胞杆菌发酵液为酶源,在水相中对映选择性催化N-苯乙酰-（R,S）-邻氯苯甘氨酸制备（S）-邻氯苯甘氨酸,当底物浓度为100mol／L时转化4h,转化率达44．2％。对底物浓度为80mmoL／L反应液中的（S）-邻氯苯甘氨酸进行分离,达到理论收率的94．29％（以N-苯乙酰-（R,S）-邻氯苯甘氨酸的0．5倍摩尔量为理论产率）,e．e．值大于99．9％。170℃条件下,N-苯乙酰-（R）-邻氯苯甘氨酸与苯乙酸共熔消旋为N-苯乙酰-（R,S）-邻氯苯甘氨酸可用于循环拆分。     

粘质沙雷氏菌产2,3-丁二醇培养基的优化

研究了各种碳源、氮源、柠檬酸及无机盐对细胞生长与产物形成的影响,通过单因子、正交及中心组合设计响应面分析优化发酵培养基。结果表明在培养基中添加柠檬酸不但可以促进细胞生长与糖耗速度,还可以缩短发酵周期,提高2,3-丁二醇的产量。采用优化后的培养基,2,3-丁二醇的产量由14.03g/L增加到39.27g/L,提高了近3倍。     

固定化耶罗维亚酵母发酵生产γ-癸内酯

目的：在发酵生产γ-癸内酯的过程中,研究固定化耶罗维亚酵母（Yarrowia lipolytica AS2.1405）,降低产物对细胞的毒性,提高γ-癸内酯的产量。方法：利用聚乙烯醇和卡拉胶固定化耶罗维亚酵母,制备出机械强度高、传质效果好的凝胶颗粒发酵生产γ-癸内酯。以小球强度和γ-癸内酯产量为主要指标,确定发酵生产γ-癸内酯的最佳条件。结果：在聚乙烯醇80g/L,卡拉胶5g/L,菌体添加量0.1g/mL,固定化时间24h,γ-癸内酯产量可达482mg/L。结论：酵母经固定化后,γ-癸内酯产量比之前提高了40%。     

谷氨酸棒状杆菌合成5-氨基乙酰丙酸的途径构建与发酵优化

5-氨基乙酰丙酸(5-amino levulinic acid,ALA)是生物体内天然存在的一种非蛋白质氨基酸,在农业和医药等领域应用广泛。为了在谷氨酸棒状杆菌中建立ALA碳四合成途径并优化其发酵体系,首先在谷氨酸棒状杆菌中过表达沼泽红假单胞菌来源的ALA合成酶(ALAS),建立高效的ALA碳四合成途径,然后从不同发酵培养基的比较、诱导剂和底物甘氨酸的浓度以及初始接种量等不同方面对ALA摇瓶发酵工艺进行了优化。结果显示,过表达Hem A的13032/p ZWA1菌株ALA产量达到1.41 g/L,是对照菌株的67.14倍。ALA的最优摇瓶发酵条件为以酵母粉为氮源的M9培养基,采用5%的接种量0.1 mmol/L IPTG进行Hem A的诱导表达,体系中甘氨酸的浓度要控制在4 g/L,摇瓶中ALA产量可达到3.28 g/L,比优化前提高了132.62%。采用发酵优化的条件,在5 L发酵罐的放大发酵中ALA产量可达10.08 g/L,这是现有报道中谷氨酸棒状杆菌一步发酵合成ALA的最高产量。     

生物转化法合成16α-羟基泼尼松龙的发酵工艺研究

目的:研究1株玫瑰产色链霉菌(Streptomyces roseochromogenes)的发酵培养基和底物转化条件,以提高16α-羟基泼尼松龙的转化率。方法:采用紫外与氯化锂复合诱变获得目的菌株TS-58,利用正交实验等方法考查摇瓶发酵条件,研究不同浓度的碳源、氮源对玫瑰产色链霉菌生长的影响,以及不同底物浓度、底物加入时间、装液量、金属离子和添加助溶剂等条件对转化生成16α-羟基泼尼松龙能力的影响。结果:获得最佳转化培养基为葡萄糖10 g/L、可溶性淀粉50 g/L、蛋白胨10 g/L、黄豆饼粉25 g/L、磷酸二氢钾0.2 g/L、硫酸镁0.5 g/L硫酸锌0.5 g/L。在底物投料量5 mg/mL添加0.8 mg/ml PEG助溶剂的最优条件下,16α-羟基泼尼松龙的转化率达到了13.8%。结论:突变株Streptomyces roseochromogenes TS-58能有效地在泼尼松龙上引入16α-羟基羟基,为工业生产16α-羟基泼尼松龙奠定了基础。     

Microbial transformation of benzene to <Emphasis Type="Italic">cis</Emphasis>-3,5-cyclohexadien-1,2-diols by recombinant bacteria harboring toluene dioxygenase gene <Emphasis Type="Italic">tod</Emphasis>

Toluene dioxygenase (TDO) catalyzes asymmetric cis-dihydroxylation of aromatic compounds. To achieve high efficient biotransformation of benzene to benzene cis-diols, Pseudomonas putida KT2442, Pseudomonas stutzeri 1317, and Aeromonas hydrophila 4AK4 were used as hosts to express TDO gene tod. Plasmid pSPM01, a derivative of broad-host plasmid pBBR1MCS-2 harboring tod from plasmid pKST11, was constructed and introduced into the above three strains. Their abilities to catalyze the biotransformation of benzene to benzene cis-diols, namely, cis-3,5-cyclohexadien-1,2-diols abbreviated as DHCD, were examined. In shake-flask cultivation under optimized culture media and growth condition, benzene cis-diols production by recombinant P. putida KT2442 (pSPM01), P. stutzeri 1317 (pSPM01), and A. hydrophila 4AK4 (pSPM01) were 2.68, 2.13, and 1.17 g/l, respectively. In comparison, Escherichia coli JM109 (pSPM01) and E. coli JM109 (pKST11) produced 0.45 and 0.53 g/l of DHCD, respectively. When biotransformation was run in a 6-l fermenter, DHCD production in P. putida KT2442 (pSPM01) was approximately 60 g/l; this is the highest DHCD production yield reported so far.     

High cell density cultivation of <Emphasis Type="Italic">Escherichia coli</Emphasis> with surface anchored transglucosidase for use as whole-cell biocatalyst for α-arbutin synthesis

A fed-batch culture strategy for the production of recombinant Escherichia coli cells anchoring surface-displayed transglucosidase for use as a whole-cell biocatalyst for α-arbutin synthesis was developed. Lactose was used as an inducer of the recombinant protein. In fed-batch cultures, dissolved oxygen was used as the feed indicator for glucose, thus accumulation of glucose and acetate that affected the cell growth and recombinant protein production was avoided. Fed-batch fermentation with lactose induction yielded a biomass of 18 g/L, and the cells possessed very high transglucosylation activity. In the synthesis of α-arbutin by hydroquinone glucosylation, the whole-cell biocatalysts showed a specific activity of 501 nkat/g cell and produced 21 g/L of arbutin, which corresponded to 76% molar conversion. A sixfold increased productivity of whole cell biocatalysts was obtained in the fed-batch culture with lactose induction, as compared to batch culture induced by IPTG.     

Addition of aromatic substrates restores trichloroethylene degradation activity in Pseudomonas putida F1

The rate of trichloroethylene (TCE) degradation by toluene dioxygenase (TDO) in resting cells of Pseudomonas putida F1 gradually decreased and eventually stopped within 1.5 h, as in previous reports. However, the subsequent addition of toluene, which is the principal substrate of TDO, resulted in its immediate degradation without a lag phase. After the consumption of toluene, degradation of TCE restarted at a rate similar to its initial degradation, suggesting that this degradation was mediated by TDO molecules that were present before the cessation of TCE degradation. The addition of benzene and cumene, which are also substrates of TDO, also caused restoration of TCE degradation activity: TCE was degraded simultaneously with cumene, and a larger amount of TCE was degraded after cumene was added than after toluene or benzene was added. But substrates that were expected to supply the cells with NADH or energy did not restore TCE degradation activity. This cycle of pseudoinactivation and restoration of TCE degradation was observed repeatedly without a significant decrease in the number of viable cells, even after six additions of toluene spread over 30 h. The results obtained in this study demonstrate a new type of restoration of TCE degradation that has not been previously reported.     

Addition of Aromatic Substrates Restores Trichloroethylene Degradation Activity in Pseudomonas putida F1

The rate of trichloroethylene (TCE) degradation by toluene dioxygenase (TDO) in resting cells of Pseudomonas putida F1 gradually decreased and eventually stopped within 1.5 h, as in previous reports. However, the subsequent addition of toluene, which is the principal substrate of TDO, resulted in its immediate degradation without a lag phase. After the consumption of toluene, degradation of TCE restarted at a rate similar to its initial degradation, suggesting that this degradation was mediated by TDO molecules that were present before the cessation of TCE degradation. The addition of benzene and cumene, which are also substrates of TDO, also caused restoration of TCE degradation activity: TCE was degraded simultaneously with cumene, and a larger amount of TCE was degraded after cumene was added than after toluene or benzene was added. But substrates that were expected to supply the cells with NADH or energy did not restore TCE degradation activity. This cycle of pseudoinactivation and restoration of TCE degradation was observed repeatedly without a significant decrease in the number of viable cells, even after six additions of toluene spread over 30 h. The results obtained in this study demonstrate a new type of restoration of TCE degradation that has not been previously reported.     

High cell density fermentation of recombinant Vibrio cholerae for the production of B subunit of Escherichia coli enterotoxin

High cell density fermentation studies were performed to produce the B subunit of Escherichia coli heat-labile enterotoxin (LTB) from a Vibrio cholerae culture that carries a recombinant plasmid with an ampicillin resistance gene, tac promoter, and the gene encoding LTB. Upon induction with isopropyl-beta-D-thiogalactopyranoside (IPTG) the culture secreted the protein into the extracellular milieu. Fed-batch fermentation with stepwise addition of a total of 5 mM of IPTG during the active growth phase of the organism resulted in the production of 400 mg/L of LTB in 9 h and a cell optical density (OD) of 24. The LTB was purified to homogeneity with 70% recovery from the fermentation broth and was found to be chemically and biologically identical to the native protein by N-terminal amino acid sequencing and receptor binding assay. (c) 1995 John Wiley & Sons, Inc.     

腈水解酶psn基因工程菌的发酵及产酶条件优化

来自恶臭假单胞菌的腈水解酶具有高效催化3-氰基吡啶产烟酸的能力,对表达该酶的基因psn进行发酵和产酶条件优化,通过对C源、N源、磷酸盐、金属离子、温度、诱导剂浓度和诱导时间进行单因素考察,获得最适培养基条件(g/L):葡萄糖5、蛋白胨15、酵母粉5、(NH4)2SO45、K2HPO424.5、KH2PO45.76、MgSO40.48;最佳诱导条件:培养2.5 h后添加IPTG诱导,浓度0.2 mmol/L,诱导温度30℃。在该条件下培养,重组大肠杆菌的腈水解酶比酶活可达到45.67 U/mL,比优化前提高了2.26倍。在此基础上,于5 L发酵罐上进行C、N源的补料研究,获得最适分批补料策略,发现其腈水解酶活力可达到75.40 U/mL,是优化前的3.74倍。     

南方红豆杉细胞悬浮培养条件优化研究

针对红豆杉细胞生长相对缓慢和培养褐化问题,本文通过正交实验和均匀实验方法并采用人工神经网络技术对南方红豆杉细胞悬浮培养条件进行优化,使细胞的生长速率和比生长速率有较大提高,并考察了细胞活性随时间的动态变化.     

抗VEGF单克隆抗体Fab片段在E.coli中的分泌表达

目的：在大肠杆菌中构建、表达和纯化抗血管内皮生长因子（VEGF）的Fab片段（兰尼单抗,ranibizumab）,通过发酵条件的控制实现其在大肠杆菌周质和胞外的高效分泌表达,并检测其抗VEGF的活性。方法：以pET30a为质粒载体,构建了Fd链和L链前都含有OmpA信号肽、SD序列和T7 promoter的克隆载体pET30a（+）-LC-HC,转化BL21（DE3）表达菌株,并进行了培养基、温度和IPTG诱导浓度的条件优化。结果：确定Fab片段在大肠杆菌分泌表达摇瓶发酵最佳条件为：在含有1.5% Tryptone,1% Yeast Extract,0.5% Glucose,0.15% NaCl,0.1% NH₄Cl,0.08% MgCl₂·6H₂O的1L培养基的摇瓶中,按照10%的接种量,37℃摇床培养至对数生长后期（OD₆₀₀为2左右）,添加0.1mmol/L IPTG诱导剂,于16℃条件下诱导表达过夜（16h左右）。用周质破菌提取分泌至大肠杆菌周质腔的Fab片段,同时用中空纤维柱浓缩发酵培养基,最后用ProteinG亲和层析柱一步纯化洗脱,经SDS-PAGE检测分析和Brandford法测蛋白浓度得出纯化的Fab抗体片段纯度在90%以上,分泌表达纯化量为0.4mg/L。以VEGF165作为结合抗原,间接ELISA分析纯化后的Fab抗体EC50=30ng/ml。继续用该培养基在3.7L体积发酵罐中进行2L体积的发酵,获得最终的菌体产率为30g/L,可亲和纯化Fab抗体量为1.94mg/L。结论：成功实现了Fab抗体片段在大肠杆菌中的高效分泌表达,且具有很高的活性,为规模化制备Fab抗体片段提供了研究依据。     

高产表面活性素的重组枯草芽孢杆菌构建及培养优化

表面活性素是一种新型生物表面活性剂,因其具有良好的表面活性、可生物降解及抗菌活性,在石油开采、医药、农业和食品化妆品等领域具有广阔的应用前景。高产表面活性素菌株的获得和发酵过程优化是其商业化生产的关键。文中考察了脂肪酸合成途径对表面活性素合成的影响,强化脂肪酸生物合成关键基因以及该途径全部基因分别构建了高产表面活性素枯草芽孢杆菌Bacillus subtilis THBS-2和THBS-8,并对发酵过程中氨基酸种类及添加量、诱导剂异丙基-β-D-硫代半乳糖苷 (IPTG) 添加时间和添加量等条件对产物合成的影响进行考察,获得优化的两阶段前体添加方案：发酵3 h,加入IPTG和L-亮氨酸,使其终浓度分别为1.25 mmol/L、5 g/L;发酵24 h,添加L-亮氨酸 (终浓度5 g/L) 和浓缩培养基5 mL。优化条件下,枯草芽孢杆菌THBS-2摇瓶发酵48 h,表面活性素产量高达24 g/L;30 L发酵罐中发酵68 h,产物产量最高达到34 g/L。研究结果为表面活性素的工业化生产及应用奠定基础。     

Kinetics of Lactococcus lactis growth and metabolite formation under aerobic and anaerobic conditions in the presence or absence of hemin

The study of batch kinetics of Lactococcus lactis cell growth and product formation reveals three distinct metabolic behaviors depending upon the availability of oxygen to the culture and the presence of hemin in the medium. These three cultivation modes, anerobic homolactic fermentation, aerobic heterolactic fermentation, and hemin-stimulated respiration have been studied at pH 6.0 and 30 degrees C with a medium containing a high concentration of glucose (60 g/L). A maximum cell density of 5.78 g/L was obtained in the batch culture under hemin-stimulated respiration conditions, about three times as much as that achieved with anerobic homolactic fermentation (1.87 g/L) and aerobic heterolactic fermentation (1.80 g/L). The maximum specific growth rate was 0.60/h in hemin-stimulated respiration, slightly higher than that achieved in homolactic fermentation (0.56/h) and substantially higher than that in heterolactic fermentation (0.40/h). Alteration of metabolism caused by the supplementation of oxygen and hemin is evidenced by changes in both cell growth kinetics and metabolite formation kinetics, which are characterized by a unique pseudo-diauxic growth of L. lactis. We hypothesise that Lactococcus lactis generates bioenergy (ATP) through simultaneous lactate formation and hemin-stimulated respiration in the primary exponential phase, when glucose is abundant, and utilizes lactate for cell growth and cell maintenance in the stationary phase, after glucose is exhausted. We also examined the applicability of a modified logistic model and the Luedeking-Piret model for cell growth kinetics and metabolite formation kinetics, respectively.