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携带运动发酵单胞菌基因的重组大肠杆菌生产乙醇

Ethanol production by recombinant Escherichia coli carrying genes from Zymomonas mobilis.

作者信息

Lawford H G, Rousseau J D

机构信息

Department of Biochemistry, University of Toronto, Ontario, Canada.

出版信息

Appl Biochem Biotechnol. 1991 Spring;28-29:221-36. doi: 10.1007/BF02922603.

Abstract

Efficient utilization of lignocellulosic feedstocks offers an opportunity to reduce the cost of producing fuel ethanol. The fermentation performance characteristics of recombinant Escherichia coli ATCC 11303 carrying the "PET plasmid" (pLOI297) with the lac operon controlling the expression of pyruvate decarboxylase (pdc) and alcohol dehydrogenase II (adhB) genes cloned from Zymomonas mobilis CP4 (Alterthum & Ingram, 1989) were assessed in batch and continuous processes with sugar mixtures designed to mimic process streams from lignocellulosic hydrolysis systems. Growth was pseudoexponential at a rate (generation time) of 1.28 h at pH 6.8 and 1.61 h at pH 6.0. The molar growth yields for glucose and xylose were 17.28 and 7.65 g DW cell/mol, respectively (at pH 6.3 and 30 degrees C), suggesting that the net yield of ATP from xylose metabolism is only 50% compared to glucose. In pH-stat batch fermentations (Luria broth with 6% sugar, pH 6.3), glucose was converted to ethanol 4-6 times faster than xylose, but the glucose conversion rate was much less than can be achieved with comparable cell densities of Zymomonas. Sugar-to-ethanol conversion efficiencies in nutrient-rich, complex LB medium were near theoretical at 98 and 88% for glucose and xylose, respectively. The yield was 10-20% less in a defined-mineral-salts medium. Acetate at a concentration of 0.1M (present in lignocellulosic hydrolysates from thermochemical processing) inhibited glucose utilization (about 50%) much more than xylose, and caused a decrease in product yield of about 30% for both sugars. With phosphate-buffered media (pH 7), glucose was a preferred substrate in mixtures with a ratio of hexose to pentose of 2.3 to 1. Xylose was consumed after glucose, and the product yield was less (0.37 g/g). Under steady-state conditions of continuous culture, the specific productivity ranged from 0.76-1.24 g EtOH/g cell/h, and the maximum volumetric productivity, 2.5 g EtOH/L/h, was achieved with a rich complex LB medium (glucose) at pH 6.0 (30 degrees C) and ethanol at 1.63% (v/v). Growth and fermentation were poor in a buffered-wood (aspen) "hemicellulose hydrolysate" containing 4% xylose and 0.1M acetate with added thiamine and mineral salts.

摘要

高效利用木质纤维素原料为降低燃料乙醇的生产成本提供了契机。对携带“PET质粒”(pLOI297)的重组大肠杆菌ATCC 11303的发酵性能特征进行了评估,该质粒带有受乳糖操纵子控制的丙酮酸脱羧酶(pdc)和乙醇脱氢酶II(adhB)基因,这两个基因是从运动发酵单胞菌CP4克隆而来(Alterthum和Ingram,1989年)。在分批和连续过程中,使用模拟木质纤维素水解系统工艺流的糖混合物进行评估。在pH 6.8时,生长呈假指数增长,速率(代时)为1.28小时;在pH 6.0时,代时为1.61小时。葡萄糖和木糖的摩尔生长产量分别为17.28和7.65克干重细胞/摩尔(在pH 6.3和30℃下),这表明木糖代谢产生的ATP净产量仅为葡萄糖的50%。在pH稳态分批发酵(含6%糖的Luria肉汤,pH 6.3)中,葡萄糖转化为乙醇的速度比木糖快4至6倍,但葡萄糖的转化率远低于运动发酵单胞菌在可比细胞密度下所能达到的转化率。在营养丰富的复杂LB培养基中,糖到乙醇的转化效率接近理论值,葡萄糖和木糖分别为98%和88%。在限定的矿物盐培养基中,产量低10 - 20%。浓度为0.1M的乙酸盐(存在于热化学处理的木质纤维素水解产物中)对葡萄糖利用的抑制作用(约50%)比对木糖的抑制作用大得多,并且两种糖的产物产量均下降约30%。对于磷酸缓冲培养基(pH 7),在己糖与戊糖比例为2.3比1的混合物中,葡萄糖是首选底物。葡萄糖消耗完后木糖才被消耗,且产物产量较低(0.37克/克)。在连续培养的稳态条件下,比生产率范围为0.76 - 1.24克乙醇/克细胞/小时,在pH 6.0(30℃)的富含复杂LB培养基(葡萄糖)和乙醇含量为1.63%(v/v)的条件下,最大体积生产率达到2.5克乙醇/升/小时。在含有4%木糖和0.1M乙酸盐并添加硫胺素和矿物盐的缓冲木材(白杨)“半纤维素水解产物”中,生长和发酵情况较差。

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