Simultaneous CO removal with renewable biofuel production can be achieved by methanogens through conversion of CO and H into CH. However, the low gas-liquid mass transfer ( ) of H limits the commercial application of this bioconversion. This study tested and compared the gas-liquid mass transfer of H by using two stirred tank reactors (STRs) equipped with a micro-nano sparger (MNS) and common micro sparger (CMS), respectively.
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