酶法合成抗病毒药物阿糖腺苷

目的:为了开发一种生产阿糖腺苷的有效方法。方法:研究了以产气肠杆菌完整细胞为催化剂酶法合成阿糖腺苷,优化了菌体培养条件以及酶反应条件。结果:在培养基中添加0.5%葡萄糖,33℃下培养16h,既能得到较多菌体,又能使菌体的催化活性保持较高。酶反应在pH7.0、25mmol/L的磷酸钾缓冲液中进行,底物浓度为阿糖尿苷30mmol/L,腺嘌呤10mmol/L,加入10%湿菌体,在60℃下振荡反应48h,腺嘌呤转化率可达90%。结论:酶法合成阿糖腺苷可应用于大规模工业化生产。     

ATP合成菌株的构建及用于联合生产S-腺苷甲硫氨酸

为降低S-腺苷甲硫氨酸的生产成本,构建了同时表达腺苷激酶、腺苷酸激酶和乙酸激酶3种酶的重组大肠杆菌菌株用于ATP的合成,并对ATP的转化条件进行了优化,优化后的反应体系为:腺苷30 mmol/L,乙酰磷酸二锂盐135 mmol/L,硫酸镁5 mmol/L,硼砂50 mmol/L,菌体2 g/L(湿重),反应液初始pH7.5,反应温度为35℃,反应时间为3 h,反应转化率可以达到99%以上。按照上述反应体系进行5 L放大,反应结束后再投入65 mmol/L D,L-甲硫氨酸和50 g/L(湿重)表达腺苷甲硫氨酸合成酶的重组大肠杆菌菌体,并补加15 mmol/L硫酸镁,转化18 h S-腺苷甲硫酸浓度能达到8.7 g/L,转化率达到72.5%。     

S-腺苷甲硫氨酸合成酶反应条件的优化

优化了重组毕赤酵母表达的S-腺苷甲硫氨酸合成酶催化L-甲硫氨酸(Met)和ATP合成 S-腺苷甲硫氨酸的条件,确定了该酶的最适酶活力检测条件为20mmol/L的L -Met,26mmol/ L的ATP,52mmol/L的MgCl2,300mmol/L的KCl,8mmol/L的还原型谷胱甘肽,100mmol/ L的Tris,反应液pH 8.5,35°C反应 1h,比活力达到23.84U/mg.该酶还可以催化以DL-Met代替L-Met为底物的S-腺苷甲硫氨酸合成反应,以降低生产成本.     

具有高谷胱甘肽合成活性重组大肠杆菌的构建及合成反应过程

以野生型大肠杆菌E.coliⅡ为宿主细胞,转化带有编码谷胱甘肽合成酶系的基因gshⅠ和gshⅡ的质粒pGH501,获得了一株谷胱甘肽合成活性、质粒稳定性和传代稳定性俱佳,并且能够重复使用的重组大肠杆菌E.coliⅡ\|1。该菌株经过甲苯处理后,能够在胞外积累4g/L左右的谷胱甘肽(GSH)。在合成反应体系中,提高L谷氨酸浓度可促进GSH合成,但L半胱氨酸浓度增大到20mmol/L后会抑制GSH的合成。根据GSH合成反应中能量辅因子的变化情况,提出E.coliⅡ\|1细胞控制的GSH合成反应机理：由谷胱甘肽合成酶(GSHⅡ)控制的第二步反应的能量供体是ADP而非ATP,该反应是整个GSH合成反应的限速步骤,高浓度ADP可能会抑制GSHⅡ的活性。在GSH合成反应体系中添加100mmol/L的L丝氨酸-硼酸钾混合物,可以有效地防止GSH的进一步降解,反应3 h后,GSH产量达到230mmol/L(约71g/L)。     

生物合成谷胱甘肽种间耦合ATP再生系统的构建

利用重组大肠杆菌Ⅱ 1中的谷胱甘肽合成酶系和面包酵母WSH J7中的ATP生物合成酶系 ,构建了一个以葡萄糖为能源的种间耦合ATP再生系统。经过通透性处理的酵母细胞几乎不能消耗葡萄糖。在反应体系中添加 1mmol/LAMP和 0 0 5mmol/LNADH ,即可启动酵母的酵解途径。提高耦合系统中的葡萄糖浓度 ,可促进GSH的合成。当葡萄糖浓度为 40 0mmol/L时 ,系统内GSH浓度达到 1 0 4mmol/L(3 2 g/L)。Mg2 +缺乏时 ,耦合系统和外加ATP的非耦合系统均不能合成谷胱甘肽。耦合系统中Mg2 +与ATP形成螯合物 ,可能是导致耦合系统中GSH产量较低的原因。在耦合系统中补加Mg2 +,反应 6h时GSH浓度达到 1 4 3mmol/L(4 4g/L)。     

S-腺苷甲硫氨酸合成酶的组成型表达、产物纯化及鉴定

将大肠杆菌(E.coli K12) S 腺苷甲硫氨酸合成酶(SAMS)基因克隆至质粒pBR322中,获得的重组质粒pBR322-SAMS转入大肠杆菌JM109菌株,构建了能高效组成型表达SAMS的重组菌E.coli JM109 (pBR322-SAMS)。将重组大肠杆菌破碎后上清液经20%~40%硫酸铵分级盐析、Phenyl-Sepharose Fast Flow疏水层析和Q Sepharose Fast Flow离子交换层析,即可得到纯度提高5倍,比活为48.7 μ/mg的SAMS,三步纯化的总回收率为62%,纯度达到92%。SAMS表达量为1 176μ/L,占到菌体可溶性总蛋白的20%。重组酶的最适反应pH为8.5,4℃下在pH 7.5的缓冲液中保温10h酶活性几乎不改变。重组酶反应的最适温度为55℃ ,酶活性稳定的温度范围为20~35℃。重组酶的KmL Met为0.22mmol/L,Vmax L-Met为1.07mmol/(L·h),Km ATP为0.52 mmol/L,Vmax ATP为1.05 mmol/( L·h)。     

基因工程菌酶法合成抗癌新药6-甲基嘌呤-2′-脱氧核苷

6-甲基嘌呤-2′-脱氧核苷(MePdR)是一种新型抗癌药物,它作为药物前体应用于PNP自杀基因治疗系统可以选择性杀伤肿瘤细胞。本实验构建了一个高效表达大肠杆菌来源的嘌呤核苷磷酸化酶重组质粒,并利用基因工程菌以15mmol/L 6-甲基嘌呤和60mmol/L 2′-脱氧尿苷为底物合成6-甲基嘌呤-2′-脱氧核苷,在40mmol/L pH7.0的磷酸缓冲液中,2%菌体在55℃反应2h,转化率可达83.78%。用硅胶制备薄层提纯得到白色针状晶体,收率为76.4%。HPLC测定该产物纯度99.3%,核磁共振鉴定该产物为MePdR。     

基因工程菌酶法合成抗癌新药6-甲基嘌呤-2'-脱氧核苷

6-甲基嘌呤-2'-脱氧核苷(MePdR)是一种新型抗癌药物,它作为药物前体应用于PNP自杀基因治疗系统可以选择性杀伤肿瘤细胞.本实验构建了一个高效表达大肠杆菌来源的嘌呤核苷磷酸化酶重组质粒,并利用基因工程菌以15mmol/L 6-甲基嘌呤和60mmol/L 2'-脱氧尿苷为底物合成6-甲基嘌呤-2'-脱氧核苷,在40mmol/L pH7.0的磷酸缓冲液中,2%菌体在55℃反应2h,转化率可达83.78%.用硅胶制备薄层提纯得到白色针状晶体,收率为76.4%.HPLC测定该产物纯度99.3%,核磁共振鉴定该产物为MePdR.     

灵菌红素缩合酶PigC在大肠杆菌中表达条件优化

灵菌红素及其类似物具有良好的抗菌性能,在新型抗菌药物开发领域具有广阔的应用前景。灵菌红素缩合酶PigC是酶法合成灵菌红素及其类似物的关键酶,为了提高重组大肠杆菌Escherichia coli BL21(DE3)/pET-32a-PigC中pigC基因的表达水平,本研究对其诱导条件进行优化。在单因素实验结果的基础上,依据Box-Behnken中心组合原则设计培养基初始pH、乳糖浓度和诱导温度的3因素3水平响应面实验,以Pig C酶活为响应值优化重组菌的诱导条件。结果表明,在培养基初始pH7.1,乳糖浓度4.2 g/L,诱导温度为16.2℃的最佳条件下,该重组菌所产PigC的最高酶活达62.4 U/mL,是优化前的4.9倍,实际值与响应面预测值拟合良好,说明通过响应面试验设计对该重组菌诱导条件的优化是有效的。本研究为PigC的制备及其酶学特性研究提供了基础资料,为酶法合成灵菌红素及其类似物提供了一定的基础。     

冻融产氨棒杆菌细胞转化法制备三磷酸腺苷

微生物发酵和酶转化法是工业上制备三磷酸腺苷(ATP)的有效途径。以腺嘌呤为关键底物,用冻融通透化处理的产氨棒杆菌细胞转化制备ATP,用高效液相色谱(HPLC)法检测ATP含量,考察各种转化条件对ATP产率的影响,确定最优转化条件:菌体用量40 g/L,底物6 g/L,葡萄糖60 g/L,Mg SO415 mmol/L,KH2PO4120 mmol/L,反应液p H 7.4,反应温度35℃。在最优转化条件下,ATP产率达到85.00%,比优化前提高了58%,细胞用量大幅度降低,优化条件稳定可行。     

Enhancement of glutathione production by altering adenosine metabolism of Escherichia coli in a coupled ATP regeneration system with Saccharomyces cerevisiae

Aims: Adenosine triphosphate (ATP) during the enzymatic production of glutathione is necessary. In this study, our aims were to investigate the reason for low glutathione production in Escherichia coli coupled with an ATP regeneration system and to develop a new strategy to improve the system. Methods and Results: Glutathione can be synthesized by enzymatic methods in the presence of ATP and three precursor amino acids (l ‐glutamic acid, l ‐cysteine and glycine). In this study, glutathione was produced from E. coli JM109 (pBV03) coupled with an ATP regeneration system, by using glycolytic pathway of Saccharomyces cerevisiae WSH2 as ATP regenerator from adenosine and glucose. In the coupled system, adenosine used for ATP regeneration by S. cerevisiae WSH2 was transformed into hypoxanthine irreversibly by E. coli JM109 (pBV03). As a consequence, S. cerevisiae WSH2 could not obtain enough adenosine for ATP regeneration in the glycolytic pathway in spite of consuming 400 mmol l^?1 glucose within 1 h. By adding adenosine deaminase inhibitor to block the metabolism from adenosine to hypoxanthine, glutathione production (8·92 mmol l^?1) enhanced 2·74‐fold in the coupled system. Conclusions: This unusual phenomenon that adenosine was transformed into hypoxanthine irreversibly by E. coli JM109 (pBV03) revealed that less glutathione production in the coupled ATP regeneration system was because of the poor efficiency of ATP generation. Significance and Impact of the Study: The results presented here provide a strategy to improve the efficiency of the coupled ATP regeneration system for enhancing glutathione production. The application potential can be microbial processes where ATP is needed.     

Enhancement of glutathione production in a coupled system of adenosine deaminase-deficient recombinant Escherichia coli and Saccharomyces cerevisiae

Adenosine triphosphate (ATP) is necessary in the enzymatic production of glutathione (GSH). Our aim was to improve GSH production by increasing the efficiency of ATP regeneration in a coupled system. Previous results suggested that low GSH production in the coupled system is due to the irreversible transformation of adenosine (Ado) to hypoxanthine (Hx) via inosine (Ino) pathway in Escherichia coli JM109 (pBV03). In this study, to block the transformation of Ado into Hx and enhance GSH production, a coupled ATP regeneration system was constructed with adenosine deaminase-deficient recombinant E. coli JW1615 (pBV03) and Saccharomyces cerevisiae WSH2. GSH production was improved (2.94-fold of the control), and ATP regeneration reaction was established in the coupled system. The results are applicable to ATP regeneration in other microbial processes.     

产1,3-丙二醇新型重组大肠杆菌的构建

利用PCR技术从大肠杆菌(Escherichia coli )中扩增出1.16 kb的编码1,3-丙二醇氧化还原酶同工酶的基因yqhD,将其连接到表达载体pEtac,得到重组载体pEtac-yqhD,重组载体在大肠杆菌JM109中得到高效表达。SDS_PAGE分析显示融合表达产物的分子量均为43 kD,同核酸序列测定所推导的值相符。对含有yqh-D的基因工程菌进行表达研究表明：37 ℃,以1.0 mmol /L IPTG诱导4 h,1,3-丙二醇氧化还原酶同工酶的酶活力达到120 u/mg蛋白,而对照菌株的酶活力为0.5 u/mg蛋白。再将含甘油脱水酶基因dhaB和含1,3-丙二醇氧化还原酶同工酶基因yqhD的重组质粒共转化大肠杆菌JM109得到重组大肠杆菌JM109（pUCtac-dhaB, pEtac-yqhD）,该菌株在好氧条件下,以1.0mmol/L IPTG诱导可将50 g/L甘油转化为38.0 g/L 1,3-丙二醇。首次发现1,3-丙二醇氧化还原酶同工酶在好氧条件下表现出较高的活性。     

Proposed mechanism of acetate accumulation in two recombinant Escherichia coli strains during high density fermentation

The productivity of Escherichia coli as a producer of recombinant proteins is affected by its metabolic properties, especially by acetate production. Two commercially used E. coli strains, BL21 (lambdaDE3) and JM109, differ significantly in their acetate production during batch fermentation at high initial glucose concentrations. E. coli BL21 grows to an optical density (OD, 600 nm) of 100 and produces no more than 2 g/L acetate, while E. coli JM109 grows to an OD (600 nm) of 80 and produces up to 14 g/L acetate. Even in fed-batch fermentation, when glucose concentration is maintained between 0.5 and 1.0 g/L, JM109 accumulates 4 times more acetate than BL21. To investigate the difference between the two strains, metabolites and enzymes involved in carbon utilization and acetate production were analyzed (isocitrate, ATP, phosphoenolpyruvate, pyruvate, isocitrate lyase, and isocitrate dehydrogenase). The results showed that during batch fermentation isocitrate lyase activity and isocitrate concentration were higher in BL21 than in JM109, while pyruvate concentration was higher in JM109. The activation of the glyoxylate shunt pathway at high glucose concentrations is suggested as a possible explanation for the lower acetate accumulation in E. coli BL21. Metabolic flux analysis of the batch cultures supports the activity of the glyoxylate shunt in E. coli BL21.     

Comparison of optimal conditions for mass production of carboxymethylcellulase by <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/A-68 with other recombinants in pilot-scale bioreactor

The optimal conditions for mass production of carboxymethylcellulase (CMCase) by E. coli JM109/A-68 were investigated and compared with other E. coli JM109 recombinants producing CMCase. The optimal agitation speed and aeration rate for cell growth of E. coli JM109/A- 68 were 500 rpm and 0.50 vvm in a 7 L bioreactor, whereas those for production of CMCase were 416 rpm and 0.95 vvm. The optimal vessel pressures for cell growth as well as production of CMCase in a 100 L bioreactor were 0.04 MPa. The maximal production of CMCase by E. coli JM109/A-68 under the optimized conditions in a 100 L bioreactor was 11.0 times higher than its wild type, B. velezensis A-68. Optimal conditions for mass production of CMCase by recombinants were different from those for wild strains. The higher production of CMCase by E. coli JM109/A-68 and other recombinant of E. coli seemed to result from its higher cell growth under the optimal conditions for dissolved oxygen and its mixed-growth associated production pattern compared to the growthassociated production of B. velezensis A-68.     

重组大肠杆菌全细胞催化合成莱鲍迪苷D

莱鲍迪苷D(Rebaudioside D,RD)是一种稀有具有高甜度的甜菊糖苷类化合物。本文实现了重组大肠杆菌全细胞催化莱鲍迪苷A(Rebaudioside A,RA)合成RD。以水稻c DNA为模板,扩增得到葡萄糖基转移酶基因eugt11,构建了重组菌株E.coli BL21(p ETDuet-eugt11),并成功表达了重组蛋白6His-EUGT11。通过Ni柱亲和层析纯化并在体外酶催化反应表征了其催化活性。将重组菌BL21(p ETDuet-eugt11)应用于催化合成RD研究。探讨了反应体系pH、温度、柠檬酸钠浓度、菌体密度、二价金属离子、二甲苯体积分数、UDPG添加浓度对反应效率的影响。单因素考察结果显示,在菌体密度0.16 g湿细胞/m L反应液,底物RA浓度为1.0 mmol/L,pH 8.0,60 mmol/L柠檬酸钠,1%二甲苯,0.1 mmol/L Zn Cl2,12.0 mmol/L UDPG,反应温度42℃,反应时间24 h的条件下,RD产量为123.6 mg/L(约0.1 mmol/L)。     

大肠杆菌BL21(pTrc-gsh)与酵母耦联合成谷胱甘肽的研究

谷胱甘肽 (ＧＳＨ)广泛存在于动、植物和微生物细胞内 ,有参与氨基酸的跨膜运输、维持细胞的还原状态等重要生理功能 ,在临床、保健品、食品等行业有广泛用途 ,如 :重金属解毒、抗氧化延缓衰老等 ,我国基本靠进口。开发高效、低成本的ＧＳＨ生产工艺势在必行。谷胱甘肽的制备有化学合成法[1 ] 、提取法[2 ] 、微生物发酵法[3] 、酶法[4] 等。由于酶法合成ＧＳＨ的产率高、后续的分离提取较简单而倍受关注。它是以ＡＴＰ为能量供体、由γ 谷氨酰半胱氨酸合成酶 (ＧＳＨＩ)和谷胱甘肽合成酶 (ＧＳＨＩＩ)连续催化合成的 :谷氨酸 半胱氨酸 Ａ…     

Statistical optimization for production of carboxymethylcellulase of <Emphasis Type="Italic">Bacillus amyloliquefaciens</Emphasis> DL-3 by a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/DL-3 from rice bran using response surface method

The optimal conditions for production of carboxymethylcellulase (CMCase) of Bacillus amyloliquefaciens DL-3 by a recombinant Escherichia coli JM109/DL-3 were established at a flask scale using the response surface method (RSM). The optimal conditions of rice bran, tryptone, and initial pH of the medium for cell growth extracted by Design Expert Software were 66.1 g/L, 6.2 g/L, and 7.2, respectively, whereas those for production of CMCase were 58.0 g/L, 5.0 g/L, and 7.1. The analysis of variance (ANOVA) of results from central composite design (CCD) indicated that significant factor (“probe > F” less than 0.0500) for cell growth was rice bran, whereas those for production of CMCase were rice bran and initial pH of the medium. The optimal temperatures for cell growth and the production of CMCase by E. coli JM109/DL-3 were found to be 37°C. The optimal agitation speed and aeration rate of 7 L bioreactors for cell growth were 498 rpm and 1.4 vvm, whereas those for production of CMCase were 395 rpm and 1.1 vvm. The ANOVA of results indicated that the aeration rate was more significant factor (“probe > F” less than 0.0001) than the agitation speed for cell growth and production of CMCase. The optimal inner pressure for cell growth was 0.08 MPa, whereas that for the production of CMCase was 0.06 MPa. The maximal production of CMCase by E. coli JM109/DL-3 under optimized conditions was 871.0 U/mL, which was 3.0 times higher than the initial production of CMCase before optimization.     

Construction of a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/A-68 for production of carboxymethylcellulase and comparison of its production with its wild type, <Emphasis Type="Italic">Bacillus velezensis</Emphasis> A-68 in a pilot-scale bioreactor

A gene encoding carboxymethylcellulase (CMCase) of Bacillus velezensis A-68 had been cloned in Escherichia coli JM109. Based on productivity and economic aspect, rice bran and ammonium chloride were chosen to be optimal carbon and nitrogen sources for production of CMCase by E. coli JM109/A-68. The optimal conditions for rice bran, ammonium chloride, and initial pH of medium for production of CMCase were established by the response surface methodology (RSM). The concentrations of four salts in the medium, K₂HPO₄, NaCl, MgSO₄·7H₂O, and (NH₄)₂SO₄, for production of CMCase also were optimized. The optimal temperatures for cell growth and production of CMCase were 37°C. The maximal production of CMCase by E. coli JM109/A-68 was 880.2 U/mL, which was 10.5 time higher than its wild type, B. velezensis A-68. The production of CMCase by E. coli JM109/A-68 was compared with that by B. velezensis A-68 in a 100 L pilot-scale bioreactor under the optimized conditions. The production of CMCase by E. coli JM109/A-68 was found to be the mixed-growth associated unlike the growthassociated production of CMCase by B. velezensis A-68.