过表达长链鞘氨醇激酶基因LCB4提高酿酒酵母抑制物耐受性

木质纤维素预处理过程中产生的有毒副产物严重影响了纤维素乙醇发酵,提高酿酒酵母抑制物耐受性是提高纤维素乙醇发酵效率的有效方法。文中通过过表达LCB4基因,研究了重组菌株S288C-LCB4在乙酸、糠醛和香草醛胁迫下的细胞生长和乙醇发酵性能。结果表明,LCB4过表达菌株在分别含有10 g/L乙酸、1.5 g/L糠醛和1 g/L香草醛的平板中生长均优于对照菌株;在分别含有10 g/L乙酸、3 g/L糠醛和2 g/L香草醛的液体乙醇发酵过程中,重组菌株S288C-LCB4乙醇发酵产率分别为0.85 g/(L·h)、0.76 g/(L·h)和1.12 g/(L·h),比对照菌株提高了34.9%、85.4%和330.8%;且糠醛和香草醛胁迫下发酵时间分别缩短了30 h和44 h。根据发酵终点发酵液代谢物分析发现重组菌株比对照菌株产生了更多甘油、海藻糖和琥珀酸,这些物质有利于增强菌株的抑制物耐受性。综上所述,LCB4基因过表达可显著提高酿酒酵母S288C在乙酸、糠醛和香草醛胁迫下的乙醇发酵性能。     

Red同源重组敲除nagE和manX对大肠杆菌发酵生产氨基葡萄糖的影响?

氨基葡萄糖(GlcN)又称氨基葡糖或葡糖胺,是葡萄糖的一个羟基被氨基取代后的化合物,在医药和保健领域具有广泛应用。在前期研究中,我们构建了一株可高效合成GlcN和其乙酰化衍生物N-乙酰氨基葡萄糖(GlcNAc)的重组大肠肝菌Escherichia coli-glms-gna1(在下游提取过程中用弱酸进行脱乙酰化即可将GlcNAc转化为GlcN)。但研究发现,发酵过程中GlcN和GlcNAc能被转运至胞内作为碳源利用,导致胞外产量显著减少。为阻断胞外GlcN和GlcNAc向胞内的转运,利用Red同源重组技术将E.coli-glms-gna1的乙酰氨基葡萄糖磷酸转运子编码基因nagE和甘露糖磷酸转运子编码基因manX敲除,获得nagE基因敲除的工程菌E.coli-glms-gna1-nagE和nagE/manX基因双敲除的工程菌E.coli-glms-gna1-nagE-manX,并在7 L发酵罐上利用构建的工程菌进行GlcN和GlcNAc的发酵生产。实验结果表明:培养对照菌株E.coli-glms-gna1至12 h时GlcN产量达到最大值4.06 g/L,GlcNAc产量达到最大值41.46 g/L;而培养单基因敲除菌株E.coli-glms-gna1-nagE至12 h时GlcN产量达到最大值4.38 g/L(是对照菌株的1.08倍),GlcNAc产量达到最大值71.80 g/L(是对照菌株的1.7倍);培养双基因敲除菌株E.coli-glms-gna1-nagE-manX至10 h时GlcN产量达到最大值4.82 g/L(是对照菌株的1.2倍),GlcNAc产量达到最大值118.78 g/L(是对照菌株的2.86倍)。这表明nagE和manX基因的敲除可显著降低GlcN和GlcNAc向胞内的转运,进而提高其在胞外的积累。研究结果对最终实现GlcN的工业化生产具有一定的指导意义。     

腺苷酸脱氨酶在乳酸克鲁维酵母中构建表达

【目的】实现鼠灰链霉菌来源经密码子优化后的腺苷酸脱氨酶基因在乳酸克鲁维酵母(Kluyveromyces lactis GG799)中组成型表达。【方法】以鼠灰链霉菌(Streptomyces murinus)来源的腺苷酸脱氨酶(AMP)基因经密码子优化后作为模板,设计特异性引物,PCR扩增AMP脱氨酶基因opt-AMPD,以p KLAC1为载体构建重组表达质粒p KLAC1-opt-AMPD,经Sac II线性化后电转化法转入K.lactis GG799,筛选得到重组菌株,测定酶活,经His TrapTM HP纯化后得到AMP脱氨酶,并优化重组菌的发酵培养基。【结果】对AMP脱氨酶基因进行了密码子优化后,构建了重组K.lactis GG799/p KLAC1-opt-AMPD,实现组成型表达,密码子优化后AMP脱氨酶酶活提高到586±50 U/m L。SDS-PAGE结果显示,纯化后的AMP脱氨酶为单一条带,蛋白大小约为60 k D。优化的发酵培养基为(g/L):葡萄糖40、蛋白胨20、酵母粉15、Na Cl 8、KCl 10、Mg SO4 2,30°C、200 r/min发酵120 h,酶活达到2 100±60 U/m L。【结论】实现了密码子优化后的腺苷酸脱氨酶基因在乳酸克鲁维酵母GG799内的组成型表达,为实现腺苷酸脱氨酶的重组高效表达和发酵生产进行了有益探索。     

一步法产1,3-丙二醇酿酒酵母基因工程菌的构建

1,3-丙二醇(1,3-PD)是一种重要的化工原料,发酵法生产1,3-PD是一条新颖且具有潜在竞争力的生产途径。本研究在前期工作的基础上,将分别来源于大肠杆菌和肺炎克雷伯氏菌的基因片段yqhD和dhaB串联表达,构建重组表达载体pYX212-zeocin-pGAP-yqhD-pGAP-dhaB;并得到重组酿酒酵母(Saccharomyces cerevisiae)W303-1A/pYX212-zeocin-pGAP-yqhD-pGAP-dhaB。该重组菌和对照S.cerevisiae分别以葡萄糖为底物摇瓶发酵72h后,重组酿酒酵母发酵液中1,3-PD含量约为1.5g/L;而对照菌株不产1,3-PD。以上结果表明本研究在国内首次成功构建了直接以葡萄糖为底物发酵生产1,3-PD的酿酒酵母基因工程菌。为进一步将dhaB、yqhD基因导入其他以葡萄糖为底物高产甘油的酵母宿主中表达,获得以葡萄糖为底物一步法发酵高产1,3-丙二醇工程菌打下了坚实的基础。     

不同的中和剂对L(+)-乳酸发酵的影响

分别利用CaCO3、6 mol/L氨水和6 mol/L NaOH溶液调控乳酸发酵过程的pH,得到的乳酸浓度为169.1g/L、187.9g/L和170.1g/L(以发酵液的初始体积计算),分别是无pH调控发酵过程的4.9倍、5.4倍和4.9倍;得到的OD620分别为19.3、21.6和16.4,分别是无pH调控(OD620为8.5)的2.3倍、2.5倍和1.9倍.相对于氨水和NaOH来说,CaCO3粉末是一种缓慢型的酸中和剂,pH调节能力有限,只能将pH维持在4.9～5.2.但CaCO3可以将乳酸以生成乳酸钙的形式沉淀下来,给下游乳酸的分离提取带来一定的方便.因此对于传统的分批式发酵,CaCO3仍不失为一种较好的选择.氨水和NaOH溶液都可以很好地将发酵液的pH调控在6.0,其中氨水是一种最理想的酸中和剂,既有利于乳酸的生物合成又能促进乳酸菌的生长.     

重组丙酮丁醇梭菌的构建及其木质纤维素ABE发酵

[目的]提高丙酮丁醇梭菌降解利用纤维素原料的能力。[方法]将甲基化的重组表达载体p SOS95-cel9电转化至丙酮丁醇梭菌ATCC824。[结果]成功构建重组菌株ATCC824/p SOS95-cel9。通过荧光定量PCR检验到外源纤维素酶基因cel9在重组丙丁梭菌中的转录,24 h的相对表达量是12 h的27. 1倍。重组菌ATCC824/p SOS95-cel9发酵滤纸产丙酮0. 05 g/L、丁醇0. 08 g/L、乙醇0. 71 g/L,发酵蔗渣水解液产0. 78 g/L、1. 09 g/L、0. 97 g/L,各溶剂产量均显著高于空质粒对照菌株。[结论]重组菌能利用滤纸及蔗渣水解液进行ABE发酵,外源纤维素酶基因cel9的重组表达提高了工程菌株利用纤维素原料的能力。     

过量表达烟酸单核苷酸腺苷酰转移酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111是敲除了乳酸脱氢酶的编码基因(ldhA)和丙酮酸-甲酸裂解酶的编码基因(pflB)的发酵生产丁二酸的潜力菌株。厌氧条件下NADH不能及时再生为NAD+,引起胞内辅酶NAD(H)的不平衡,最终导致厌氧条件下菌株不能利用葡萄糖生长代谢。nadD为催化NAD(H)合成途径中烟酸单核苷酸(NaMN)生成烟酸腺嘌呤二核苷酸(NaAD)的烟酸单核苷酸腺苷酰转移酶(Nicotinic acid mononucleotide adenylyltransferase,NAMNAT)的编码基因,通过过量表达nadD基因能够提高NAD(H)总量与维持合适的NADH/NAD+比例。文中构建了重组菌E.coli NZN111/pTrc99a-nadD,在厌氧摇瓶发酵过程中通过添加终浓度为1.0 mmol/L的IPTG诱导表达,重组菌E.coli NZN111/pTrc99a-nadD中NAD+和NADH的浓度分别比宿主菌E.coli NZN111提高了3.21倍和1.67倍,NAD(H)总量提高了2.63倍,NADH/NAD+从0.64降低为0.41,使重组菌株恢复了厌氧条件下生长和代谢葡萄糖的能力。重组菌与对照菌相比,72 h内可以消耗14.0 g/L的葡萄糖产6.23 g/L的丁二酸,丁二酸产量增加了19倍。     

产丁二酸工程菌的构建及其厌氧发酵

为了考察过量表达苹果酸酶对于E.coli NZN111(ldhA::Kan pfl::Cam)厌氧发酵产丁二酸的影响, 将连接有苹果酸酶基因sfcA的表达载体pTrc99a-sfcA转化进NZN111中, 构建了重组NZN111(pTrc99a-sfcA)。0.5 mmol/L IPTG诱导8 h后, 测定的苹果酸酶比酶活为30.67 u/mg, 比受体菌提高了140倍。采用两阶段发酵模式, 结果表明: 过量表达的苹果酸酶在NZN111体内催化了从丙酮酸到苹果酸的逆向反应, 丁二酸是发酵过程中积累的主要有机酸, 且当加入0.7 mmol/L IPTG诱导, 初始葡萄糖糖浓度为18.5 g/L时, 选择对数生长期后期的菌种以10%的接种量转入厌氧发酵, 发酵结束时发酵液中丁二酸的浓度为12.84 g/L, 对葡萄糖的收率为69.43%, 乙酸为0.58 g/L, 二者浓度比为22:1, 没有检测到甲酸和乳酸。构建的菌种具有高产丁二酸和副产物极少的优点, 在同类菌种中处于先进水平。     

HCMV pp65截短蛋白原核表达条件优化

为了提高HCMVpp65蛋白片段在大肠杆菌中表达量,研究了不同发酵条件对其表达的影响,包括培养基、接种量、温度、摇床转速、pH、诱导时间以及诱导剂IPTG使用浓度等。结果表明,以LB培养基为发酵液,按5%接种量,37℃培养3h后IPTG诱导5h,重组菌菌体生物量为0.6g/L,目的蛋白表达量达18mg/L。用3.7L发酵罐进行放大培养,菌体生物量达0.85g/L,最高目的蛋白表达量达到25mg/L。     

大肠杆菌琥珀酸和乙酸合成途径的删除及其重组菌株的D-乳酸发酵

菌株CICIM B0013-030 (B0013,ack-pta,pps,pflB) 可积累D-乳酸作为主要发酵产物,然而副产物琥珀酸和乙酸的含量分别高达乳酸的11.9％和7.1％。为构建副产物含量低的产D-乳酸重组大肠杆菌菌株,本研究删除了菌株B0013-030的琥珀酸 (frdA) 和乙酸 (tdcDE) 合成途径,并考察了重组菌株在摇瓶和发酵罐中经两阶段发酵 (好氧生长菌体和厌氧发酵产酸) 利用葡萄糖发酵D-乳酸的性能。结果表明,分别构建含有frdA::difGm和tdcDE::difGm突变盒的重组质粒,并利用Red重组系统将突变盒整合于染色体上的目的基因,再利用Xer重组系统去除抗生素抗性基因,依次获得了重组菌株B0013-040B (B0013-030,frdA) 和B0013-050B (B0013-040B,tdcDE)。摇瓶发酵结果表明,frdA基因的删除使得菌株B0013-040B副产物琥珀酸的含量降低了80.8％;在7 L发酵罐中进行乳酸发酵,菌株B0013-040B的D-乳酸产量达114.5 g/L,光学纯度大于99.9％,但仍积累1.0 g/L琥珀酸和5.4 g/L乙酸。进一步删除了tdcD和tdcE基因的菌株B0013-050B,在7 L发酵罐中生产111.9 g/L D-乳酸,乙酸和琥珀酸的合成量分别降低为0.4 g/L,其他副产物含量也维持较低水平,表明该菌株具有较优良的D-乳酸发酵性能。     

烟酸转磷酸核糖激酶和丙酮酸羧化酶共表达对大肠杆菌BA002产丁二酸的影响

大肠杆菌BA002是敲除了乳酸脱氢酶的编码基因 (ldhA) 和丙酮酸-甲酸裂解酶的编码基因 (pflB) 的工程菌。厌氧条件下NADH不能及时再生为NAD+,引起胞内辅酶NAD(H)的不平衡,最终导致厌氧条件下菌株不能利用葡萄糖生长代谢。pncB是烟酸转磷酸核糖激酶 (NAPRTase) 的编码基因,通过过量表达pncB基因能够提高NAD(H)总量与维持合适的NADH/NAD+,从而恢复了厌氧条件下重组菌E. coli BA014 (BA002/pTrc99a-pncB) 的生长和产丁二酸的性能。然而,BA014在厌氧发酵过程中有大量丙酮酸积累,为进一步提高菌株的丁二酸生产能力,减少副产物丙酮酸的生成,共表达NAPRTase和来自于乳酸乳球菌 NZ9000中丙酮酸羧化酶 (PYC) 的编码基因pyc,构建了重组菌E. coli BA016 (BA002/pTrc99a-pncB-pyc)。3 L发酵罐结果表明,BA016发酵112 h后,共消耗了35.00 g/L的葡萄糖。发酵结束时,菌体OD600为4.64,产生了25.09 g/L丁二酸。通过共表达pncB和pyc基因,使BA016的丙酮酸积累进一步降低,丁二酸产量进一步提高。     

rIL-2工程菌诱导阶段细胞再循环培养的研究

为了减少rIL-2工程菌高密度培养时乙酸的积累,在诱导阶段对该工程菌进行细胞再循环培养的研究,比较了细胞再循环补料液、pH、细胞循环培养时间段对工程菌的生长及rIL-2表达的影响。结果表明在菌密度D_(600)为50时,细胞再循环补料液中酵母抽提物与胰蛋白胨浓度为发酵培养基的5倍就能满足rIL-2表达的需求,同时选择诱导后4～6h之间的细胞再循环培养能有效地防止乙酸的过高积累并减少营养物质的损失,有利于rIL-2的表达。根据以上研究结果得到了rIL-2工程菌诱导阶段细胞再循环培养方法,使得在诱导前菌密度D_(600)为50左右时rIL-2的表达水平约为40％。     

共表达烟酸转磷酸核糖激酶和丙酮酸羧化酶对大肠杆菌NZN111产丁二酸的影响

构建了共表达烟酸转磷酸核糖激酶(NAPRTase)和丙酮酸羧化酶(PYC)的重组质粒pTrc99a-pncB-pyc,并考察了重组菌E.coli NZN111/pTrc99a-pncB-pyc生产丁二酸的能力。结果表明:重组菌NZN111/pTrc99a-pncB-pyc的NAPRTase和PYC的比酶活达到最高,分别为20.75和1.04 U/mg,同时,辅酶NADH、NAD+及NAD(H)总量达到最高。厌氧摇瓶发酵结果:48 h能够消耗17.5 g/L的葡萄糖生成14.08 g/L的丁二酸,而丙酮酸的产量大幅度降低,仅为0.11 g/L。本研究为基因工程菌大肠杆菌厌氧条件下发酵生产丁二酸提供了一定的基础。     

Control of amino sugar metabolism in Escherichia coli and isolation of mutants unable to degrade amino sugars

1. Growth of Escherichia coli on glucosamine results in an induction of glucosamine 6-phosphate deaminase [2-amino-2-deoxy-d-glucose 6-phosphate ketol-isomerase (deaminating), EC 5.3.1.10] and a repression of glucosamine 6-phosphate synthetase (l-glutamine-d-fructose 6-phosphate aminotransferase, EC 2.6.1.16); glucose abolishes these control effects. 2. Growth of E. coli on N-acetylglucosamine results in an induction of N-acetylglucosamine 6-phosphate deacetylase and glucosamine 6-phosphate deaminase, and in a repression of glucosamine 6-phosphate synthetase; glucose diminishes these control effects. 3. The synthesis of amino sugar kinases (EC 2.7.1.8 and 2.7.1.9) is unaffected by growth on amino sugars. 4. Glucosamine 6-phosphate synthetase is inhibited by glucosamine 6-phosphate. 5. Mutants of E. coli that are unable to grow on N-acetylglucosamine have been isolated, and lack either N-acetylglucosamine 6-phosphate deacetylase (deacetylaseless) or glucosamine 6-phosphate deaminase (deaminaseless). Deacetylaseless mutants can grow on glucosamine but deaminaseless mutants cannot. 6. After growth on glucose, deacetylaseless mutants have a repressed glucosamine 6-phosphate synthetase and a super-induced glucosamine 6-phosphate deaminase; this may be related to an intracellular accumulation of acetylamino sugar that also occurs under these conditions. In one mutant the acetylamino sugar was shown to be partly as N-acetylglucosamine 6-phosphate. Deaminaseless mutants have no abnormal control effects after growth on glucose. 7. Addition of N-acetylglucosamine or glucosamine to cultures of a deaminaseless mutant caused inhibition of growth. Addition of N-acetylglucosamine to cultures of a deacetylaseless mutant caused lysis, and secondary mutants were isolated that did not lyse; most of these secondary mutants had lost glucosamine 6-phosphate deaminase and an uptake mechanism for N-acetylglucosamine. 8. Similar amounts of (14)C were incorporated from [1-(14)C]-glucosamine by cells of mutants and wild-type growing on broth. Cells of wild-type and a deaminaseless mutant incorporated (14)C from N-acetyl[1-(14)C]glucosamine more efficiently than from N[1-(14)C]-acetylglucosamine, incorporation from the latter being further decreased by acetate; cells of a deacetylaseless mutant showed a poor incorporation of both types of labelled N-acetylglucosamine.     

Metabolic flux analysis for succinic acid production by recombinant Escherichia coli with amplified malic enzyme activity

A pfl ldhA double mutant Escherichia coli strain NZN111 was used to produce succinic acid by overexpressing the E. coli malic enzyme. Escherichia coli strain NZN111 harboring pTrcML produced 6 and 8 g/L of succinic acid from 20 g/L of glucose in flask culture at 37 degrees C and 30 degrees C, respectively. When NZN111(pTrcML) was cultured at 30 degrees C with intermittent glucose feeding the final succinic acid concentration obtained was 9.5 g/L and the ratio of succinic acid to acetic acid was 13:1. This system could not be analyzed by conventional metabolic flux analysis techniques, since some pyruvate and succinic acid were accumulated intracellularly. Therefore, a new flux analysis method was proposed by introducing intracellular pyruvate and succinic acid pools. By this new method the concentrations of intracellular metabolites were successfully predicted and the differences between the measured and calculated reaction rates could be considerably reduced.     

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.     

Relieving effects of glycine and methionine from acetic acid inhibition in Escherichia coli fermentation

Among amino acids screened for their potential to relieve wild and recombinant Escherichia coli from the negative effects of acetic acid, glycine, and methionine showed a sparing effect. In the presence of 2 g/L of acetic acid, addition of 0.5 g/L of glycine or methionine resulted in either a complete recovery or a further enhancement in the specific growth rate, while the enhancement was significant but not fully complete in the presence of 4 g/L of acetic acid. The addition of 0.5 g/L of methionine alleviated the negative effect of acetic acid on recombinant E. Coli growth to produce more beta-lactamase, which was encoded by plasmid pUC18. In continuous fermentation the methionine effect on recombinant. E. coli metabolism depended on dilution rate; at high dilution rates, above 0.4 h(-1), the methionine addition enhanced beta-lactamase production and reduced acetic acid formation, while at low dilution rates, below 0.3 h (-1), the effect was reversed. In def-batch fermentation with wild-type E. Coli, cell growth rate and cell yield from glucose were enhanced with methionine addition, while the acetic acid concentration reached over 4 g/L. (c) 1993 John Wiley & Sons, Inc.     

Directed evolution and characterization of Escherichia coli glucosamine synthase

Glucosamine synthase (GlmS) converts fructose-6-phosphate to glucosamine-6-phosphate. Overexpression of GlmS in Escherichia coli increased synthesis of glucosamine-6-P, which was dephosphorylated and secreted as glucosamine into the growth medium. The E. coli glmS gene was improved through error-prone polymerase chain reaction (PCR) in order to develop microbial strains for fermentation production of glucosamine. Mutants producing higher levels of glucosamine were identified by a plate cross-feeding assay and confirmed in shake flask cultures. Over 10 mutants were characterized and all showed significantly reduced sensitivity to inhibition by glucosamine-6-phosphate. Ki of mutants ranged from 1.4 to 4.0 mM as compared to 0.56 mM for the wild type enzyme. Product resistance resulted from single mutations (L468P, G471S) and/or combinations of mutations in the sugar isomerase domain. Most overexpressed GlmS protein was found in the form of inclusion bodies. Cell lysate from mutant 2123-72 contained twice as much soluble GlmS protein and enzyme activity as the strain overexpressing the wild type gene. Using the product-resistant mutant, glucosamine production was increased 60-fold.     

Engineering of unconventional yeast Yarrowia lipolytica for efficient succinic acid production from glycerol at low pH

Yarrowia lipolytica is considered as a potential candidate for succinic acid production because of its innate ability to accumulate citric acid cycle intermediates and its tolerance to acidic pH. Previously, a succinate-production strain was obtained through the deletion of succinate dehydrogenase subunit encoding gene Ylsdh5. However, the accumulation of by-product acetate limited further improvement of succinate production. Meanwhile, additional pH adjustment procedure increased the downstream cost in industrial application. In this study, we identified for the first time that acetic acid overflow is caused by CoA-transfer reaction from acetyl-CoA to succinate in mitochondria rather than pyruvate decarboxylation reaction in SDH negative Y. lipolytica. The deletion of CoA-transferase gene Ylach eliminated acetic acid formation and improved succinic acid production and the cell growth. We then analyzed the effect of overexpressing the key enzymes of oxidative TCA, reductive carboxylation and glyoxylate bypass on succinic acid yield and by-products formation. The best strain with phosphoenolpyruvate carboxykinase (ScPCK) from Saccharomyces cerevisiae and endogenous succinyl-CoA synthase beta subunit (YlSCS2) overexpression improved succinic acid titer by 4.3-fold. In fed-batch fermentation, this strain produced 110.7 g/L succinic acid with a yield of 0.53 g/g glycerol without pH control. This is the highest succinic acid titer achieved at low pH by yeast reported worldwide, to date, using defined media. This study not only revealed the mechanism of acetic acid overflow in SDH negative Y. lipolytica, but it also reported the development of an efficient succinic acid production strain with great industrial prospects.     

碱胁迫下耐碱植物星星草体内柠檬酸特异积累现象(英)

对碱胁迫 (0 - 175mmol/LNa2 CO3 )下星星草 (Puccinelliatenuiflora (Griseb .)Scribn .etMerr.)体内柠檬酸的积累规律及其相关胁变指标进行分析测定。实验结果证明 :积累柠檬酸是星星草对碱胁迫特有的生理反应。盐胁迫(0 - 4 0 0mmol/LNaCl)下 ,柠檬酸含量反而稍有下降。柠檬酸积累量随碱胁迫强度增大而增大 ,低胁迫强度时积累量上升缓慢 ,当胁迫强度大于 10 0mmol/LNa2 CO3 时 ,积累量明显上升。柠檬酸积累与胁迫时间之间呈直角曲线关系 ,一定胁迫强度下胁迫 4h后即可测出柠檬酸含量明显上升 ,约 4 8h后渐趋最大值。碱胁迫 14 4h后星星草各部位中柠檬酸含量从高到低的顺序依次是老叶、成熟叶、老叶鞘、幼叶鞘、幼茎、老茎和幼叶。成熟叶中柠檬酸随碱胁迫强度增大而逐渐上升 ,老叶和叶鞘中的柠檬酸在碱胁迫强度大于 12 5mmol/L后急剧上升 ,茎中柠檬酸含量无明显增高 ,幼叶中柠檬酸含量基本不变。实验证明 ,碱胁迫下积累的主要是柠檬酸 ,其他有机酸无明显变化。