Thiele Jurgen H, Zeikus J Gregory
Michigan Biotechnology Institute, P.O. Box 27609, Lansing, Michigan 48909, and the Departments of Biochemistry and Microbiology, Michigan State University, East Lansing, Michigan 48824.
Appl Environ Microbiol. 1988 Jan;54(1):20-29. doi: 10.1128/aem.54.1.20-29.1988.
Microbial formate production and consumption during syntrophic conversion of ethanol or lactate to methane was examined in purified flocs and digestor contents obtained from a whey-processing digestor. Formate production by digestor contents or purified digestor flocs was dependent on CO(2) and either ethanol or lactate but not H(2) gas as an electron donor. During syntrophic methanogenesis, flocs were the primary site for formate production via ethanol-dependent CO(2) reduction, with a formate production rate and methanogenic turnover constant of 660 muM/h and 0.044/min, respectively. Floc preparations accumulated fourfold-higher levels of formate (40 muM) than digestor contents, and the free flora was the primary site for formate cleavage to CO(2) and H(2) (90 muM formate per h). Inhibition of methanogenesis by CHCl(3) resulted in formate accumulation and suppression of syntrophic ethanol oxidation. H(2) gas was an insignificant intermediary metabolite of syntrophic ethanol conversion by flocs, and its exogenous addition neither stimulated methanogenesis nor inhibited the initial rate of ethanol oxidation. These results demonstrated that >90% of the syntrophic ethanol conversion to methane by mixed cultures containing primarily Desulfovibrio vulgaris and Methanobacterium formicicum was mediated via interspecies formate transfer and that <10% was mediated via interspecies H(2) transfer. The results are discussed in relation to biochemical thermodynamics. A model is presented which describes the dynamics of a bicarbonate-formate electron shuttle mechanism for control of carbon and electron flow during syntrophic methanogenesis and provides a novel mechanism for energy conservation by syntrophic acetogens.
在从乳清处理消化器获得的纯化絮体和消化器内容物中,研究了乙醇或乳酸向甲烷的互营转化过程中微生物甲酸盐的产生和消耗情况。消化器内容物或纯化的消化器絮体产生甲酸盐取决于二氧化碳以及乙醇或乳酸,但不依赖氢气作为电子供体。在互营产甲烷过程中,絮体是通过乙醇依赖的二氧化碳还原产生甲酸盐的主要场所,甲酸盐产生速率和产甲烷周转常数分别为660 μM/h和0.044/min。絮体制备物中甲酸盐积累水平比消化器内容物高四倍(40 μM),而游离菌群是甲酸盐裂解为二氧化碳和氢气的主要场所(每小时90 μM甲酸盐)。三氯甲烷对产甲烷的抑制导致甲酸盐积累并抑制互营乙醇氧化。氢气是絮体互营乙醇转化过程中微不足道的中间代谢产物,外源添加氢气既不刺激产甲烷,也不抑制乙醇氧化的初始速率。这些结果表明,主要含有普通脱硫弧菌和甲酸甲烷杆菌的混合培养物将互营乙醇转化为甲烷的过程中,>90%是通过种间甲酸盐转移介导的,<10%是通过种间氢气转移介导的。结合生化热力学对结果进行了讨论。提出了一个模型,该模型描述了用于控制互营产甲烷过程中碳和电子流动的碳酸氢盐 - 甲酸盐电子穿梭机制的动力学,并为互营产乙酸菌的能量守恒提供了一种新机制。