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嗜热栖热放线菌利用重复分批培养从氢气和二氧化碳生产乙酸盐和乙醇。

Acetate and ethanol production from H2 and CO2 by Moorella sp. using a repeated batch culture.

作者信息

Sakai Shinsuke, Nakashimada Yutaka, Inokuma Kentaro, Kita Masayuki, Okada Hideki, Nishio Naomichi

机构信息

Department of Molecular Biotechnology, Graduate School of Advanced Sciences of Matter, Hiroshima University, 1-3-1 Kagamiyama, Higashi-Hiroshima 739-8530, Japan.

出版信息

J Biosci Bioeng. 2005 Mar;99(3):252-8. doi: 10.1263/jbb.99.252.

Abstract

The growth inhibition of Moorella sp. HUC22-1 by undissociated acetic acid was analyzed using a non-competitive inhibition model coupled with a pH inhibition model. In the cells grown on H2 and CO2, the inhibition constant, K(p) of the undissociated acetic acid was 6.2 mM (164 mM as the total acetate at pH 6.2, pKa = 4.795, 55 degrees C), which was 1.5-fold higher than that obtained in cells grown on fructose. When a pH-controlled batch culture was performed using a fermentor at pH 6.2 with H2 and CO2, a maximum of 0.92 g/l of dry cell weight and 339 mM of acetate were produced after 220 h, which were 4.4- and 6.8-fold higher than those produced in the pH-uncontrolled batch culture, respectively. In order to reduce acetate inhibition in the culture medium, a repeated batch culture with cell recycling was performed at a constant pH with H2 and CO2. At a pH of 6.2, the total acetate production reached 840 mmol/l-reactor with 4.7 mmol/l-reactor of total ethanol production after 420 h. When the culture pH was maintained at 5.8, which was the optimum for ethanol production, the total ethanol production reached 15.4 mmol/l-reactor after 430 h, although the total acetate production was decreased to 675 mmol/l-reactor.

摘要

使用非竞争性抑制模型与pH抑制模型相结合的方法,分析了未解离乙酸对嗜热栖热放线菌(Moorella sp.)HUC22-1的生长抑制作用。在以H2和CO2为底物生长的细胞中,未解离乙酸的抑制常数K(p)为6.2 mM(在pH 6.2、pKa = 4.795、55℃条件下,总乙酸盐为164 mM),比在以果糖为底物生长的细胞中得到的抑制常数高1.5倍。当使用发酵罐在pH 6.2条件下,以H2和CO2进行pH控制的分批培养时,220小时后,最大干细胞重量为0.92 g/l,乙酸盐浓度为339 mM,分别比未控制pH的分批培养中产生的干细胞重量和乙酸盐浓度高4.4倍和6.8倍。为了减少培养基中乙酸盐的抑制作用,在恒定pH条件下,以H2和CO2进行了带有细胞循环的重复分批培养。在pH 6.2时,420小时后,总乙酸盐产量达到840 mmol/l-反应器,总乙醇产量为4.7 mmol/l-反应器。当培养pH维持在5.8(乙醇生产的最佳pH)时,430小时后,总乙醇产量达到15.4 mmol/l-反应器,尽管总乙酸盐产量降至675 mmol/l-反应器。

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