4.8 Article

Bubble coalescence suppression driven carbon monoxide (CO)-water mass transfer increase by electrolyte addition in a hollow fiber membrane bioreactor (HFMBR) for microbial CO conversion to ethanol

期刊

BIORESOURCE TECHNOLOGY
卷 263, 期 -, 页码 375-384

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.biortech.2018.05.012

关键词

Gas-liquid mass transfer; Bubble coalescence; Syngas fermentation; Carbon monoxide; Bioethanol

资金

  1. New & Renewable Energy Core Technology Program of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) - Ministry of Trade, Industry and Energy [20173010092460]
  2. C1 Gas Refinery Program through the National Research Foundation of Korea (NRF) - Ministry of Science and FP7 Information and Communication Technologies [NRF-2015M3D3A1A01064883]

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This study investigated the effects of electrolytes (CaCl2, K2HPO4, MgSO4, NaCl, and NH4Cl) on CO mass transfer and ethanol production in a HFMBR. The hollow fiber membranes (HFM) were found to generate tiny gas bubbles; the bubble coalescence was significantly suppressed in electrolyte solution. The volumetric gas-liquid mass transfer coefficients (k(L)a) increased up to 414% compared to the control. Saturated CO (C*) decreased as electrolyte concentrations increased. Overall, the maximum mass transfer rate (R-max) in electrolyte solution ranged from 106% to 339% of the value obtained in water. The electrolyte toxicity on cell growth was tested using Clostridium autoethanogenum. Most electrolytes, except for MgSO4, inhibited cell growth. The HFMBR operation using a medium containing 1% MgSO4 achieved 119% ethanol production compared to that without electrolytes. Finally, a kinetic simulation using the parameters got from the 1% MgSO4 medium predicted a higher ethanol production compared to the control.

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