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Coproduction of Acetaldehyde and Hydrogen during Glucose Fermentation by Escherichia coli

机译:大肠杆菌葡萄糖发酵过程中乙醛和氢的联产

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摘要

Escherichia coli K-12 strain MG1655 was engineered to coproduce acetaldehyde and hydrogen during glucose fermentation by the use of exogenous acetyl-coenzyme A (acetyl-CoA) reductase (for the conversion of acetyl-CoA to acetaldehyde) and the native formate hydrogen lyase. A putative acetaldehyde dehydrogenase/acetyl-CoA reductase from Salmonella enterica (SeEutE) was cloned, produced at high levels, and purified by nickel affinity chromatography. In vitro assays showed that this enzyme had both acetaldehyde dehydrogenase activity (68.07 ± 1.63 μmol min−1 mg−1) and the desired acetyl-CoA reductase activity (49.23 ± 2.88 μmol min−1 mg−1). The eutE gene was engineered into an E. coli mutant lacking native glucose fermentation pathways (ΔadhE, ΔackA-pta, ΔldhA, and ΔfrdC). The engineered strain (ZH88) produced 4.91 ± 0.29 mM acetaldehyde while consuming 11.05 mM glucose but also produced 6.44 ± 0.26 mM ethanol. Studies showed that ethanol was produced by an unknown alcohol dehydrogenase(s) that converted the acetaldehyde produced by SeEutE to ethanol. Allyl alcohol was used to select for mutants with reduced alcohol dehydrogenase activity. Three allyl alcohol-resistant mutants were isolated; all produced more acetaldehyde and less ethanol than ZH88. It was also found that modifying the growth medium by adding 1 g of yeast extract/liter and lowering the pH to 6.0 further increased the coproduction of acetaldehyde and hydrogen. Under optimal conditions, strain ZH136 converted glucose to acetaldehyde and hydrogen in a 1:1 ratio with a specific acetaldehyde production rate of 0.68 ± 0.20 g h−1 g−1 dry cell weight and at 86% of the maximum theoretical yield. This specific production rate is the highest reported thus far and is promising for industrial application. The possibility of a more efficient “no-distill” ethanol fermentation procedure based on the coproduction of acetaldehyde and hydrogen is discussed.
机译:大肠杆菌K-12菌株MG1655经过工程改造,可通过使用外源性乙酰辅酶A(乙酰辅酶A)还原酶(用于将乙酰辅酶A转化为乙醛)和天然甲酸盐氢裂解酶在葡萄糖发酵过程中共同产生乙醛和氢。从肠沙门氏菌(SeEutE)克隆了一个假定的乙醛脱氢酶/乙酰辅酶A还原酶,高产量生产,并通过镍亲和色谱纯化。体外试验表明,该酶既具有乙醛脱氢酶活性(68.07±1.63μmolmin -1 mg -1 ),又具有所需的乙酰辅酶A还原酶活性(49.23±2.88)。 μmolmin -1 mg -1 )。将eutE基因工程化为缺乏天然葡萄糖发酵途径(ΔadhE,ΔackA-pta,ΔldhA和ΔfrdC)的大肠杆菌突变体。工程菌株(ZH88)产生4.91±0.29 mM乙醛,同时消耗11.05 mM葡萄糖,但同时产生6.44±0.26 mM乙醇。研究表明,乙醇是由未知的乙醇脱氢酶产生的,该酶将SeEutE产生的乙醛转化为乙醇。烯丙醇用于选择具有降低的醇脱氢酶活性的突变体。分离了三个耐烯丙醇的突变体;与ZH88相比,所有产品产生的乙醛更多,乙醇更少。还发现通过添加1g酵母提取物/升和将pH降低至6.0来修饰生长培养基进一步增加了乙醛和氢的联产。在最佳条件下,菌株ZH136以1:1的比例将葡萄糖转化为乙醛和氢,比乙醛的生产率为0.68±0.20 gh -1 g -1 干电池重量和最大理论收率的86%。该特定生产率是迄今为止报道的最高生产率,有望在工业上应用。讨论了基于乙醛和氢气共同生产的更有效的“无蒸馏”乙醇发酵程序的可能性。

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