三酶级联催化L-苏氨酸生产L-2-氨基丁酸

L-2-氨基丁酸(L-ABA)是一种重要的化工原材料和手性医药中间体,为了实现L-ABA的高效生产,本研究在大肠杆菌EscherichiacoliBL21(DE3)中分别表达大肠杆菌来源的苏氨酸脱氨酶(Threonine deaminase,TD)、苏云金芽孢杆菌来源的亮氨酸脱氢酶(Leucine dehydrogenase,LDH)和博伊丁假丝酵母来源的甲酸脱氢酶(Formatedehydrogenase,FDH),构建体外级联酶催化反应实现L-苏氨酸向L-ABA的转化,体系中TD、LDH和FDH添加最适比例为1∶1∶0.2。为了简化生产工艺,将3种酶在一株菌E. coli 3FT+L中共表达并实现上述配比,在30 L发酵罐中用E. coli 3FT+L全细胞转化12 h,L-ABA的产量为68.5 g/L,底物L-苏氨酸的摩尔转化率达到99.0%。该工艺路线绿色高效,为未来大规模生产L-ABA提供借鉴。     

亮氨酸脱氢酶C端Loop区域的理性设计及多酶级联高效合成l-2-氨基丁酸

亮氨酸脱氢酶 (Leucine dehydrogenase,LDH) 是制备l-2-氨基丁酸的关键限速酶,针对该酶的Loop区域进行改造以提高关键酶的酶活及稳定性从而高效合成l-2-氨基丁酸。通过亮氨酸脱氢酶的分子动力学模拟分析均方根涨落 (Root mean square fluctuation,RMSF) 值,对其波动非常明显的Loop区域合理设计以得到比酶活提高的截短突变体EsLDHD2,其比酶活为野生型的123.2%;此外,由于l-2-氨基丁酸制备过程中苏氨酸脱氨酶催化l-苏氨酸制备2-酮丁酸的速率过快导致多酶催化不平衡,因此双拷贝亮氨酸脱氢酶及甲酸脱氢酶以平衡多酶催化速率,构建多酶级联催化的单细胞E. coli BL21/pACYCDuet-RM,其摩尔转化率相较于E. coli BL21/pACYCDuet-RO提高74.6%;对菌株E. coli BL21/pACYCDuet-RM的全细胞转化条件进行优化,其最适pH、温度、底物浓度分别为7.5、35 ℃和80 g/L,此时摩尔转化率大于99%;在1 L转化体系和最适转化条件下分批加入l-苏氨酸80 g和40 g,l-2-氨基丁酸的产量达97.2 g。总之,该策略为l-2-氨基丁酸的制备提供了绿色、高效的合成方法,具有工业化制备药物前体的巨大潜力。     

亮氨酸脱氢酶偶联NADH再生体系合成L-2-氨基丁酸

文中以大肠杆菌BL21(DE3)为宿主,构建两株分别共表达亮氨酸脱氢酶(LDH,来源蜡样芽孢杆菌)/甲酸脱氢酶(FDH,来源水生弯杆菌)和亮氨酸脱氢酶(LDH,来源蜡样芽孢杆菌)/醇脱氢酶(ADH,来源红球菌)的重组大肠杆菌。通过偶联两种不同NADH再生体系,以L-苏氨酸为起始原料,利用苏氨酸脱氨酶(L-TD)与LDH-FDH或LDH-ADH一锅法合成L-2-氨基丁酸,并对LDH-FDH工艺和LDH-ADH工艺进行对比优化。LDH-FDH工艺的最适反应pH为7.5,最适反应温度为35℃,通过加入50 g/L甲酸铵、0.3 g/L NAD+、10%LDH-FDH粗酶液(V/V)和7 500 U/L的L-TD酶液,对L-苏氨酸进行分批补加,以便控制2-丁酮酸浓度小于15 g/L,反应28 h,实现了L-2-氨基丁酸的产量为161.8 g/L,产率97%。LDH-ADH工艺的最适pH为8.0,最适反应温度为35℃,通过加入0.3 g/L NAD+、10%LDH-ADH粗酶液(V/V)及7 500 U/L的L-TD酶液,分批补加L-苏氨酸及1.2倍摩尔量异丙醇,以便控制2-丁酮酸浓度小于15g/L,且每生成约40g/L的L-2-氨基丁酸,抽真空去除丙酮,反应24h,实现了L-2-氨基丁酸的产量为119.6 g/L,产率98%。文中所采用的工艺及结果可为L-2-氨基丁酸的工业化提供一定的参考依据。     

(S)-羰基还原酶Ⅱ与葡萄糖脱氢酶共催化高效合成(S)-苯乙二醇北大核心CSCD

【目的】通过优化获得最佳酶活配比,设计近平滑假丝酵母(Candida parapsilosis)CCTCC M203011的(S)-羰基还原酶Ⅱ与枯草芽孢杆菌(Bacillus sp.)YX-1葡萄糖脱氢酶在大肠杆菌中的共表达体系,实现重组菌高效催化2-羟基苯乙酮,合成(S)-苯乙二醇。【方法】分别从重组大肠杆菌中纯化了(S)-羰基还原酶Ⅱ和葡萄糖脱氢酶,研究了2种酶共催化2-羟基苯乙酮的最佳酶活比例,最适催化温度和pH,由此构建(S)-羰基还原酶Ⅱ和葡萄糖脱氢酶的共表达体系。【结果】(S)-羰基还原酶Ⅱ的比酶活力为1.3 U/mg,葡萄糖脱氢酶的比酶活力为13.5 U/mg。在总酶活力为1 U时,(S)-羰基还原酶Ⅱ和葡萄糖脱氢酶共催化体系中,确定了2种酶的最佳比例在1∶1到5∶1(U/U)之间,最适反应温度为30℃,pH为7.0。在此基础上构建了(S)-羰基还原酶Ⅱ和葡萄糖脱氢酶基因比为1∶1的共表达体系,共表达重组菌破碎上清液中(S)-羰基还原酶Ⅱ和葡萄糖脱氢酶酶活分别为0.76 U/mg和0.73 U/mg,两者的酶活比例为1∶1。在上述确定的最适催化条件下,其催化10 g/L 2-羟基苯乙酮,产物(S)-苯乙二醇的光学纯度和得率均高达99%以上。与仅含有(S)-羰基还原酶Ⅱ的重组大肠杆菌相比,共表达体系转化产物(S)-苯乙二醇的得率明显提高,且转化时间由原来的24 h缩短为13 h。【结论】通过确定(S)-羰基还原酶Ⅱ和葡萄糖脱氢酶最佳酶活配比,为构建手性催化的靶酶和辅酶再生酶共表达体系,为实现手性化合物的高效制备提供了研究基础。     

多酶组合催化制备L-高苯丙氨酸

【目的】L-高苯丙氨酸(L-HPA)是许多医药化学品的重要中间体,化学合成法生产L-HPA反应复杂、环境污染严重,本研究旨在开发高效环保的L-HPA酶法合成路线。【方法】采用模块化组装的方法,构建了一条以甘氨酸和苯乙醛为底物高产L-HPA的新途径。【结果】首先,根据文献挖掘设计了一条由苏氨酸醛缩酶(TA)、苏氨酸脱氨酶(TD)、苯丙氨酸脱氢酶(PheDH)和甲酸脱氢酶(FDH)组成的多酶组合催化途径,用于L-HPA的合成。其次,根据氨基基团的引入和重构,将L-HPA多酶组合催化途径分为基础单元和扩增单元,基础单元包括TA和TD,扩增单元包括PheDH和FDH。然后,利用不同表达水平的质粒,对基础单元和扩增单元进行蛋白表达的组合调节,获得最优工程菌BL21-C-M1-R-M2,使L-HPA产量达到208.6mg/L。最后,我们对全细胞转化体系进行优化,使L-HPA产量进一步提高到1226.6 mg/L,苯乙醛摩尔转化率为34.2%。【结论】该工艺路线绿色高效,为未来大规模生产L-HPA奠定基础。     

内消旋-二氨基庚二酸脱氢酶不对称合成非天然手性D-氨基酸的研究进展

内消旋-二氨基庚二酸脱氢酶不对称合成非天然的手性D-氨基酸是目前生物催化领域的研究热点。内消旋-二氨基庚二酸脱氢酶具有优良的立体选择性,利用其进行酶催化不对称合成光学纯的手性D-氨基酸,被广泛用于医药、食品、化妆品、精细化学品等领域。为了促进生物催化法在合成手性D-氨基酸方向的进一步发展,本文对内消旋-二氨基庚二酸脱氢酶催化合成D-氨基酸的现状进行了综述。重点介绍了Corynebacterium glutamicum、Ureibacillus thermosphaericus、Symbiobacterium thermophilum来源的内消旋-二氨基庚二酸脱氢酶在新酶的挖掘、催化性能、晶体结构解析、分子改造、功能与催化机制、合成D-氨基酸新途径等方面的研究进展,并对内消旋-二氨基庚二酸脱氢酶的未来研究方向及策略进行了展望。本综述将进一步加深人们对内消旋-二氨基庚二酸脱氢酶的认识,也为具有挑战性的生物合成任务提供信息借鉴。     

重组大肠杆菌全细胞催化L-苏氨酸合成2,5-二甲基吡嗪

2,5-二甲基吡嗪 (2,5-dimethylpyrazine,2,5-DMP) 在食品香料与医药方面具有重要的经济价值,工业上普遍采用环境不友好且反应条件苛刻的化学合成法来生产。文中结合代谢工程和辅因子工程策略设计高效催化L-苏氨酸合成2,5-DMP的全细胞催化剂,实现微生物转化法合成2,5-DMP。本研究首先分析了不同微生物来源的苏氨酸脱氢酶 (Threonine dehydrogenase,TDH) 对2,5-DMP合成的影响,发现来源于大肠杆菌Escherichia coli中EcTDH具有最佳的催化能力,2,5-DMP产量达到 (438.3±23.7) mg/L。随后结合辅因子工程,通过引入乳脂链球菌Lactococcus cremoris中NADH氧化酶 (NADH oxidase,LcNoxE) 并优化其表达方式发现通过融合表达EcTDH和LcNoxE可平衡胞内NADH/NAD+水平,维持较高细胞存活率,进一步提高2,5-DMP产量。最后,通过阻断合成2,5-DMP的支路代谢途径,可以显著减少副产物积累,增加2,5-DMP产量,同时提高L-苏氨酸转化率。最终获得的重组菌EcΔkΔAΔBΔA/TDHEcNoxELc-PSstT在含有5 g/L L-苏氨酸的转化体系中于37 ℃、200 r/min孵化24 h,可积累 (1 095.7±81.3) mg/L的2,5-DMP,L-苏氨酸转化率达到76%,产物得率为0.288 g/(g L-苏氨酸)。因此,文中构建的重组菌可以实现高效催化L-苏氨酸合成2,5-DMP,具有一定的工业应用潜力。     

苹果S6PDH基因克隆与原核表达

6-磷酸山梨醇脱氢酶(sorbitol-6-phosphate dehydrogenase,S6PDH)是蔷薇科植物中合成山梨醇的重要酶。以苹果叶片为材料,利用RT-PCR法克隆到S6PDHcDNA全长,将其与大肠杆菌表达载体pET-32a( )构建原核表达载体pET-S并转化大肠杆菌BL21,经IPTG诱导表达后,SDS-PAGE检测结果表明该基因表达了1个约54kD的蛋白,为进一步研究目的蛋白的结构和功能提供了试验基础。     

基于双酶级联协调表达策略高效催化合成D-甘露醇北大核心CSCD

D-甘露醇(D-mannitol)作为合成抗肿瘤药和免疫刺激剂的重要前体被广泛应用于制药和医疗等行业,酶法合成D-甘露醇反应成本昂贵无法满足工业化生产。本研究首先筛选关键酶获得较优性能的甘露醇脱氢酶Lp MDH和用于辅因子NADH再生的葡萄糖脱氢酶Ba GDH,在大肠杆菌(Escherichia coli)BL21(DE3)中共表达,实现了基于双酶级联反应催化底物D-果糖合成D-甘露醇,D-甘露醇的初步摩尔转化率为59.7%。针对双酶级联催化反应中辅酶再生用酶与催化用酶表达量不协调的问题,通过增加Bagdh拷贝量来提高辅因子循环能力,获得了双酶催化速率平衡的重组大肠杆菌E.coli BL21/pETDuet-Lpmdh-Bagdh-Bagdh。进一步对重组菌的全细胞转化条件进行优化,确定了最适转化条件为反应温度30℃,初始pH值6.5,菌体量OD600=30,底物D-果糖100.0 g/L,辅底物葡萄糖与底物1︰1摩尔当量。于最优转化条件下5 L发酵罐转化24 h,D-甘露醇的最高产量为81.9g/L,摩尔转化率为81.9%。本研究提供了一种绿色、高效生物催化生产D-甘露醇的方法,为实现其规模化生产奠定了基础,同时也对其他相关稀有糖醇的研究具有指导意义。     

Bacillus megaterium WZ009催化合成(R)-4-氯-3-羟基丁酸乙酯和(S)-3-羟基-γ-丁内酯

以外消旋4-氯-3-羟基丁酸乙酯为唯一C源的富集培养筛选得到一株菌株WZ009,经16S rDNA测序鉴定为巨大芽胞杆菌(Bacillus megaterium)。B.megaterium WZ009静息细胞可以立体选择性催化(S)-4-氯-3-羟基丁酸乙酯水解和脱氯反应得到光学纯的(R)-4-氯-3-羟基丁酸乙酯(e.e.≥99%)和(S)-3-羟基-γ-丁内酯(e.e.≥95%)。笔者对B.megaterium WZ009不对称催化反应影响因素(温度、pH、中和剂、底物浓度、时间进程以及细胞重复利用)进行优化研究,确定了该反应体系最优条件:底物浓度200 mmol/L,中和剂氨水,pH 7.2,40℃反应12 h,转化率达到50.6%,底物对映体过量值为99.6%。该生物催化合成(R)-4-氯-3-羟基丁酸乙酯和(S)-3-羟基-γ-丁内酯过程具有良好的工业化应用前景。     

Regulation of folate-mediated one-carbon metabolism by 10-formyltetrahydrofolate dehydrogenase

10-Formyltetrahydrofolate dehydrogenase (FDH) catalyzes the NADP(+)-dependent conversion of 10-formyltetrahydrofolate to CO(2) and tetrahydrofolate (THF) and is an abundant high affinity folate-binding protein. Although several activities have been ascribed to FDH, its metabolic role in folate-mediated one-carbon metabolism is not well understood. FDH has been proposed to: 1) inhibit purine biosynthesis by depleting 10-formyl-THF pools, 2) maintain cellular folate concentrations by sequestering THF, 3) deplete the supply of folate-activated one-carbon units, and 4) stimulate the generation of THF-activated one-carbon unit synthesis by channeling folate cofactors to other folate-dependent enzymes. The metabolic functions of FDH were investigated in neuroblastoma, which do not contain detectable levels of FDH. Both low and high FDH expression reduced total cellular folate concentrations by 60%, elevated rates of folate catabolism, and depleted cellular 5-methyl-THF and S-adenosylmethionine levels. Low FDH expression increased the formyl-THF/THF ratio nearly 10-fold, whereas THF accounted for nearly 50% of total folate in neuroblastoma with high FDH expression. FDH expression did not affect the enrichment of exogenous formate into methionine, serine, or purines and did not suppress de novo purine nucleotide biosynthesis. We conclude that low FDH expression facilitates the incorporation of one-carbon units into the one-carbon pool, whereas high levels of FDH expression deplete the folate-activated one-carbon pool by catalyzing the conversion of 10-formyl-THF to THF. Furthermore, FDH does not increase cellular folate concentrations by sequestering THF in neuroblastoma nor does it inhibit or regulate de novo purine biosynthesis. FDH expression does deplete cellular 5-methyl-THF and S-adenosylmethionine levels indicating that FDH impairs the folate-dependent homocysteine remethylation cycle.     

甲酸脱氢酶及其在手性生物制造中的应用

氧化还原生物合成体系在绿色生物制造手性化合物中具有重要应用价值.甲酸脱氢酶(formate dehydrogenase,FDH)能氧化甲酸盐生成二氧化碳,同时将NAD(P)+还原为NAD(P)H,是氧化还原生物合成中辅酶再生体系的关键酶.但天然的FDH催化效率低、稳定性差、辅酶利用率不高等缺点制约了其在工业生产中的应用...     

Antipolarity in the ilv operon of Escherichia coli K-12

The genes governing three of the enzymes of the isoleucine-valine biosynthetic pathway form the operon: operator-ilvA-ilvD-ilvE. The enzymes are: ilvA, l-threonine deaminase; ilvD, dihydroxy acid dehydrase; and ilvE, transaminase B. A nonsense mutation in the ilvD gene (D-ochre) and a nonsense mutation in the ilvE gene (E-amber) affect the properties of the proximal gene product, l-threonine deaminase (TD), in addition to inactivating the enzymes produced by the genes in which the mutations have occurred. The D-ochre mutation causes TD to move in diffusion and gel filtration experiments as though it were 30% smaller than the wild-type enzyme. The E-amber mutation causes TD to move in similar experiments as though it were much larger than the wild-type enzyme. Both mutations completely abolish the sensitivity of TD to l-isoleucine, the normal feedback inhibitor of the wild-type enzyme. The effects of the nonsense mutations on TD can be reversed in three ways: by genetic reversion of the D-ochre mutation; by treatment of the altered enzymes with 3.0 m urea; and by forming a heterozygous diploid, containing the wild-type allele as well as the mutant allele of ilvD or ilvE. The results suggest that the subunits of TD undergo abnormal aggregation in the presence of the partial polypeptides produced by the mutant alleles of ilvD or ilvE; multi-enzyme aggregates in extracts of wild type, however, could not be detected.     

甲醛氧化途径关键酶重组蛋白的生化特性及固定化酶吸收甲醛效果研究

甲醛脱氢酶(formaldehyde dehydrogenase,ADH)与甲酸脱氢酶(formate dehydrogenase,FDH)是甲醛氧化途径的两个关键酶.恶臭假单胞菌(Pseudomonas putida)的PADH是一种不依赖谷胱甘肽可以把游离甲醛直接氧化为甲酸的脱氢酶,博伊丁假丝酵母菌(Candida boidinii)的FDH在有NAD+存在时可以把甲酸氧化为二氧化碳.以基因组DNA为模板用PCR方法,从P.putida中扩增出PADH基因的编码区(padh),从C.boidinii中扩增出FDH的编码区(fdh),然后亚克隆到pET-28a(+)中分别构建这两个基因的原核表达载体pET-28a-padh和pET-28a-fdh,转化大肠杆菌,利用IPTG诱导重组蛋白PADH和FDH的表达.通过优化条件使重组蛋白的表达量占菌体总蛋白的70%以上,通过亲和层析法纯化出可溶性PADH和FDH重组蛋白.对重组蛋白的生化特性分析结果表明:PADH在最适反应温度50℃的活性为1.95 U/mg;FDH在最适反应温度40℃的活性为0.376 U/mg.所表达的重组蛋白与之前报道过的相比,具有更好的热稳定性和更广的温度适应范围.将PADH、FDH两个重组蛋白及辅因子NAD+固定到聚丙烯酰胺载体基质上,对固定化酶甲醛吸收效果的初步分析结果显示固定化酶对空气中的甲醛有一定的吸收效果,说明这两种酶被固定后具有开发成治理甲醛污染环保产品的潜力.     

Synthesis of optically active amino acids from alpha-keto acids with Escherichia coli cells expressing heterologous genes.

We describe a simple method for enzymatic synthesis of L and D amino acids from alpha-keto acids with Escherichia coli cells which express heterologous genes. L-amino acids were produced with thermostable L-amino acid dehydrogenase and formate dehydrogenase (FDH) from alpha-keto acids and ammonium formate with only an intracellular pool of NAD+ for the regeneration of NADH. We constructed plasmids containing, in addition to the FDH gene, the genes for amino acid dehydrogenases, including i.e., leucine dehydrogenase, alanine dehydrogenase, and phenylalanine dehydrogenase. L-Leucine, L-valine, L-norvaline, L-methionine, L-phenylalanine, and L-tyrosine were synthesized with the recombinant E. coli cells with high chemical yields (> 80%) and high optical yields (up to 100% enantiomeric excess). Stereospecific conversion of various alpha-keto acids to D amino acids was also examined with recombinant E. coli cells containing a plasmid coding for the four heterologous genes of the thermostable enzymes D-amino acid aminotransferase, alanine racemase, L-alanine dehydrogenase, and FDH. Optically pure D enantiomers of glutamate and leucine were obtained.     

10-formyltetrahydrofolate dehydrogenase requires a 4'-phosphopantetheine prosthetic group for catalysis

10-Formyltetrahydrofolate dehydrogenase (FDH) consists of two independent catalytic domains, N- and C-terminal, connected by a 100-amino acid residue linker (intermediate domain). Our previous studies on structural organization and enzymatic properties of rat FDH suggest that the overall enzyme reaction, i.e. NADP(+)-dependent conversion of 10-formyltetrahydrofolate to tetrahydrofolate and CO(2), consists of two steps: (i) hydrolytic cleavage of the formyl group in the N-terminal catalytic domain, followed by (ii) NADP(+)-dependent oxidation of the formyl group to CO(2) in the C-terminal aldehyde dehydrogenase domain. In this mechanism, it was not clear how the formyl group is transferred between the two catalytic domains after the first step. This study demonstrates that the intermediate domain functions similarly to an acyl carrier protein. A 4'-phosphopantetheine swinging arm bound through a phosphoester bond to Ser(354) of the intermediate domain transfers the formyl group between the catalytic domains of FDH. Thus, our study defines the intermediate domain of FDH as a novel carrier protein and provides the previously lacking component of the FDH catalytic mechanism.     

Improving the purification of NAD+-dependent formate dehydrogenase from Candida methylica

The Candida methylica (cm) recombinant wild type formate dehydrogenase (FDH) gene has been cloned into the pQE-2 TAGZyme expression vector and the 6xHis-tagged FDH gene has been overexpressed in JM105 cells to purify the FDH protein more efficiently, by the use of exopeptidases, TAGZyme Purification System, which has allowed the complete removal of the small N-terminal His-tag. After the purification procedure, 1.2 mg/mL cmFDH protein of >95% purity was obtained. The kinetic parameters of cmFDH have been determined by observing the oxidation of the nicotinamide coenzyme at 340 nm. The results have also been compared to the yield of standard vs. affinity purification of FDH.