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首页> 外文期刊>Applied and Environmental Microbiology >Inhibition of the Fermentation of Propionate to Methane by Hydrogen, Acetate, and Propionate
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Inhibition of the Fermentation of Propionate to Methane by Hydrogen, Acetate, and Propionate

机译:氢,乙酸和丙酸酯对丙酸酯发酵甲烷的抑制作用

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Inhibition of the fermentation of propionate to methane and carbon dioxide by hydrogen, acetate, and propionate was analyzed with a mesophilic propionate-acclimatized sludge that consisted of numerous flocs (size, 150 to 300 μm). The acclimatized sludge could convert propionate to methane and carbon dioxide stoichiometrically without accumulating hydrogen and acetate in a propionate-minimal medium. Inhibition of propionate utilization by propionate could be analyzed by a second-order substrate inhibition model (shown below) given that the substrate saturation constant, Ks, was 15.9 μM; the substrate inhibition constant, Ki, was 0.79 mM; and the maximum specific rate of propionate utilization, qm, was 2.15 mmol/g of mixed-liquor volatile suspended solids (MLVSS) per day: qs = qmS/[Ks + S + (S2/Ki)], where qs is the specific rate of propionate utilization and S is the initial concentration of undissociated propionic acid. For inhibition by hydrogen and acetate to propionate utilization, a noncompetitive product inhibition model was used: qs = qm/[1 + (P/Kp)n], where P is the initial concentration of hydrogen or undissociated acetic acid and Kp is the inhibition constant. Kinetic analysis gave, for hydrogen inhibition, Kp(H2) = 0.11 atm (= 11.1 kPa, 71.5 μM), qm = 2.40 mmol/g of MLVSS per day, and n = 1.51 and, for acetate inhibition, Kp(HAc) = 48.6 μM, qm = 1.85 mmol/g of MLVSS per day, and n = 0.96. It could be concluded that the increase in undissociated propionic acid concentration was a key factor in inhibition of propionate utilization and that hydrogen and acetate cooperatively inhibited propionate degradation, suggesting that hydrogenotrophic and acetoclastic methanogens might play an important role in enhancing propionate degradation to methane and carbon dioxide.
机译:用中温的丙酸适应性污泥分析了丙酸被氢气,乙酸盐和丙酸发酵为甲烷和二氧化碳的过程,该污泥由许多絮状物组成(大小为150至300μm)。驯化的污泥可以将丙酸盐化学计量地转化为甲烷和二氧化碳,而不会在丙酸盐最小介质中积聚氢和乙酸盐。给定底物饱和常数Ks为15.9μM,可以通过二级底物抑制模型(如下所示)分析丙酸酯对丙酸利用的抑制作用。底物抑制常数Ki为0.79 mM;丙酸利用率的最大比值qm为每天2.15 mmol / g混合液挥发性悬浮固体(MLVSS):qs = qmS / [Ks + S +(S2 / Ki)],其中qs为比值丙酸酯利用率和S为未解离丙酸的初始浓度。为了抑制氢和乙酸对丙酸的利用,使用了非竞争性产物抑制模型:qs = qm / [1 +(P / Kp)n],其中P是氢或未解离的乙酸的初始浓度,Kp是抑制量不变。动力学分析得出,对于氢抑制而言,Kp(H2)= 0.11 atm(= 11.1 kPa,71.5μM),qm =每天MLVSS 2.40 mmol / g,n = 1.51;对于乙酸酯抑制而言,Kp(HAc)= 48.6μM,每天qm = 1.85 mmol / g MLVSS,n = 0.96。可以得出结论,未解离的丙酸浓度的增加是抑制丙酸盐利用的关键因素,氢和乙酸盐协同抑制丙酸盐的降解,表明氢营养和乙破产甲烷菌可能在促进丙酸盐降解为甲烷和碳方面起重要作用。二氧化碳。

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