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工艺参数对大肠杆菌W3110中琥珀酸产量及参与还原性三羧酸循环的酶的影响。

Effect of process parameters on succinic acid production in Escherichia coli W3110 and enzymes involved in the reductive tricarboxylic acid cycle.

作者信息

Isar Jasmine, Agarwal Lata, Saran Saurabh, Gupta Pritesh, Saxena Rajendra Kumar

机构信息

Department of Microbiology, University of Delhi South Campus, New Delhi, India.

出版信息

Can J Microbiol. 2006 Sep;52(9):893-902. doi: 10.1139/w06-034.

Abstract

The effect of process optimization on succinic acid production by Escherichia coli W3110 and on enzymes involved in the reverse tricarboxylic acid cycle was studied. Approximately, 7.02 g L-1 of succinic acid was produced in 60 h at pH 7.0 in 500 mL anaerobic bottles containing 300 mL of the medium, wherein the sucrose concentration was 2.5%, the ratio of tryptone to ammonium hydrogen phosphate was 1:1, and the concentration of magnesium carbon ate was 1.5%. When these optimized fermentation conditions were employed in a 10 L bioreactor, 11.2 g L-1 of succinic acid was produced in 48 h. This is a 10-fold increase in succinic acid production from the initial titer of 0.94 g L-1. This clearly indicates the importance of process optimization, where by manipulating the media composition and production conditions, a remarkable increase in the production of the desired biomolecule can be obtained. The production of succinic acid is a multi-step reaction through the reverse tricarboxylic acid cycle. A linear relationship was observed between succinic acid production and the enzyme activities. The enzyme activities were found to increase in the order phospho-enol-pyruvate carboxylase<malate dehydrogenase<fumarase<fumarate reductase. The activity of phospho-enol-pyruvate carboxykinase was also estimated. Results indicate that this enzyme was not a very active participant in the production of succinic acid, since it catalyzes the phosphorylation of oxaloacetic acid to yield phospho-enol-pyruvate.

摘要

研究了工艺优化对大肠杆菌W3110琥珀酸产量以及参与反向三羧酸循环的酶的影响。在含有300 mL培养基的500 mL厌氧瓶中,于pH 7.0条件下培养60 h,大约产生了7.02 g L-1的琥珀酸,其中蔗糖浓度为2.5%,胰蛋白胨与磷酸氢铵的比例为1:1,碳酸镁浓度为1.5%。当在10 L生物反应器中采用这些优化的发酵条件时,48 h内产生了11.2 g L-1的琥珀酸。这是从初始滴度0.94 g L-1的琥珀酸产量增加了约10倍。这清楚地表明了工艺优化的重要性,即通过控制培养基组成和生产条件,可以显著提高所需生物分子的产量。琥珀酸的产生是通过反向三羧酸循环的多步反应。观察到琥珀酸产量与酶活性之间存在线性关系。发现酶活性按磷酸烯醇丙酮酸羧化酶<苹果酸脱氢酶<延胡索酸酶<延胡索酸还原酶的顺序增加。还估计了磷酸烯醇丙酮酸羧激酶的活性。结果表明,该酶在琥珀酸产生过程中不是非常活跃的参与者,因为它催化草酰乙酸磷酸化生成磷酸烯醇丙酮酸。

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