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一种同时供气和细胞回收的反应(SGCR)系统,可实现微生物一氧化碳发酵中的生物质促进和高乙酸盐产量。

A simultaneous gas feeding and cell-recycled reaction (SGCR) system to achieve biomass boosting and high acetate titer in microbial carbon monoxide fermentation.

机构信息

School of Earth Sciences and Environmental Engineering, Gwangju Institute of Science and Technology (GIST), Gwangju 61005, Republic of Korea.

Bioenergy & Environmental Sustainable Technology (BEST) Research Group, Department of Chemical Engineering, COMSATS Institute of Information Technology (CIIT), Lahore, Pakistan.

出版信息

Bioresour Technol. 2020 Feb;298:122549. doi: 10.1016/j.biortech.2019.122549. Epub 2019 Dec 4.

Abstract

This study employed a simultaneous gas feeding and cell-recycled reaction (SGCR) system to ferment CO using Eubacterium limosum KIST612. A bubble column reactor was equipped with an ex-situ hollow fiber membrane module to enable cell recycling. The internal gas circulation rate was adjusted by controlling the pump speed to provide sufficient gas supplement to the microorganism. Gas feedings were conducted by either the use of a gas-tight bag (Batch), a pressurized gas cylinder (Continuous), or a sequential combination of the two (Mixed feeding). Mixed feeding mode achieved higher biomass (9.7 g/L) and acetate (9.8 g/L) concentrations than Batch mode (3.2 g/L biomass and 7.0 g/L acetate) or Continuous mode (5.0 g/L biomass and 8.1 g/L acetate). The high acetate titer in Mixed feeding mode was achieved due to the high concentration of cells secured in a short time at the initial operation stage and maintaining a high specific growth rate.

摘要

本研究采用同时供气和细胞循环反应(SGCR)系统,利用产琥珀酸丝状杆菌 KIST612 发酵 CO。鼓泡柱式反应器配备了一个外置中空纤维膜组件,以实现细胞循环。通过控制泵的速度来调节内部气体循环率,为微生物提供充足的气体补充。供气方式分别采用气密袋(Batch)、加压钢瓶(Continuous)或两者的顺序组合(Mixed feeding)。与 Batch 模式(生物量 3.2 g/L,乙酸盐 7.0 g/L)或 Continuous 模式(生物量 5.0 g/L,乙酸盐 8.1 g/L)相比,混合进料模式实现了更高的生物量(9.7 g/L)和乙酸盐(9.8 g/L)浓度。在混合进料模式下,乙酸盐的高浓度是由于在初始操作阶段短时间内获得了高浓度的细胞,并保持了较高的比生长速率。

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