Department of Fermentation Technology, Faculty of Engineering, Hiroshima University, Saijo-cho, Higashi-Hiroshima 724, Japan.
Appl Environ Microbiol. 1990 Mar;56(3):719-23. doi: 10.1128/aem.56.3.719-723.1990.
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 mum). 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, K(s), was 15.9 muM; the substrate inhibition constant, K(i), was 0.79 mM; and the maximum specific rate of propionate utilization, q(m), was 2.15 mmol/g of mixed-liquor volatile suspended solids (MLVSS) per day: q(s) = q(m)S/[K(s) + S + (S/K(i))], where q(s) 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: q(s) = q(m)/[1 + (P/K(p))], where P is the initial concentration of hydrogen or undissociated acetic acid and K(p) is the inhibition constant. Kinetic analysis gave, for hydrogen inhibition, K(p(H(2))) = 0.11 atm (= 11.1 kPa, 71.5 muM), q(m) = 2.40 mmol/g of MLVSS per day, and n = 1.51 and, for acetate inhibition, K(p(HAc)) = 48.6 muM, q(m) = 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.
在嗜温条件下,用由大量絮体(大小为 150 至 300 微米)组成的丙酸驯化污泥分析了氢、乙酸和丙酸对丙酸向甲烷和二氧化碳发酵的抑制作用。在丙酸最小化培养基中,驯化污泥可以将丙酸转化为甲烷和二氧化碳,而不会积累氢和乙酸。由于底物饱和常数 K(s)为 15.9 μM;底物抑制常数 K(i)为 0.79 mM;以及丙酸利用的最大比速率 q(m)为 2.15 mmol/g 混合液挥发性悬浮固体(MLVSS)/天,可以通过二级底物抑制模型分析丙酸利用的抑制作用:q(s) = q(m)S/[K(s) + S + (S/K(i))],其中 q(s)是丙酸利用的比速率,S 是未解离丙酸的初始浓度。对于氢和乙酸对丙酸利用的抑制作用,使用非竞争性产物抑制模型:q(s) = q(m)/[1 + (P/K(p))],其中 P 是氢或未解离乙酸的初始浓度,K(p)是抑制常数。动力学分析表明,对于氢抑制,K(p(H(2))) = 0.11 大气压(= 11.1 kPa,71.5 μM),q(m) = 2.40 mmol/g MLVSS/天,n = 1.51;对于乙酸抑制,K(p(HAc)) = 48.6 μM,q(m) = 1.85 mmol/g MLVSS/天,n = 0.96。可以得出结论,未解离丙酸浓度的增加是抑制丙酸利用的关键因素,氢和乙酸协同抑制丙酸降解,这表明氢营养型和乙酸营养型产甲烷菌可能在增强丙酸向甲烷和二氧化碳的降解中发挥重要作用。