提高挥发性脂肪酸生产的顺序间歇式反应器:微生物种群和生长动力学评价

Jing Xiang. Lim, V. Vadivelu
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引用次数: 10

摘要

采用工作体积为8 L、交换比为20%的序批式反应器(SBR)对生产挥发性脂肪酸的微生物进行富集。该处理系统抑制了利用产甲烷菌的挥发性脂肪酸(VFA)的生长,提高了VFA的产量。强化反应器在不产生甲烷气体的情况下实现了VFA的稳定积累。生料中VFA的平均产量比原始VFA含量高43.8%。在达到稳定状态后,进行16S宏基因组分析鉴定SBR中的物种。此外,通过批量实验测定了富集微生物的生长动力学。其衰减系数(bD)和生物量产量(Y)分别为0.1665天和0.174 mg生物量/mg COD消耗。最大特定生长率(μmax)为0.636 day-1,半饱和常数(Ks)为12752 mgCOD/L。采用工作体积为8 L、交换比为20%的序批式反应器(SBR)对生产挥发性脂肪酸的微生物进行富集。该处理系统抑制了利用产甲烷菌的挥发性脂肪酸(VFA)的生长,提高了VFA的产量。强化反应器在不产生甲烷气体的情况下实现了VFA的稳定积累。生料中VFA的平均产量比原始VFA含量高43.8%。在达到稳定状态后,进行16S宏基因组分析鉴定SBR中的物种。此外,通过批量实验测定了富集微生物的生长动力学。其衰减系数(bD)和生物量产量(Y)分别为0.1665天和0.174 mg生物量/mg COD消耗。最大特定生长率(μmax)为0.636 day-1,半饱和常数(Ks)为12752 mgCOD/L。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Enhanced volatile fatty acid production in sequencing batch reactor: Microbial population and growth kinetics evaluation
A sequencing batch reactor (SBR) with a working volume of 8 L and an exchange ratio of 20% was used to enrich microorganism for the production of volatile fatty acid. The treatment system managed to suppress the growth of volatile fatty acid (VFA)-utilising methanogen and increased the VFA output. The enhancement reactor managed to achieve stable accumulation of VFA without producing methane gas. The average VFA production was 43.8 % more than that of the original VFA content in raw POME. After achieving steady state, 16S metagenomic analysis was conducted to identify the species in the SBR. Further, the growth kinetic of the enriched microorganism were determined in batch experiments. The decay coefficient (bD) and biomass yield (Y) were found to be 0.1665 day-1 and 0.174 mg biomass/mg COD consumed, respectively. The maximum specific growth rate (μmax) was estimated to be 0.636 day-1 while the half saturation constant (Ks) with respect to COD was determined to be 12752 mgCOD/L.A sequencing batch reactor (SBR) with a working volume of 8 L and an exchange ratio of 20% was used to enrich microorganism for the production of volatile fatty acid. The treatment system managed to suppress the growth of volatile fatty acid (VFA)-utilising methanogen and increased the VFA output. The enhancement reactor managed to achieve stable accumulation of VFA without producing methane gas. The average VFA production was 43.8 % more than that of the original VFA content in raw POME. After achieving steady state, 16S metagenomic analysis was conducted to identify the species in the SBR. Further, the growth kinetic of the enriched microorganism were determined in batch experiments. The decay coefficient (bD) and biomass yield (Y) were found to be 0.1665 day-1 and 0.174 mg biomass/mg COD consumed, respectively. The maximum specific growth rate (μmax) was estimated to be 0.636 day-1 while the half saturation constant (Ks) with respect to COD was determined to be 12752 mgCOD/L.
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