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Fig. 7 | Biotechnology for Biofuels and Bioproducts

Fig. 7

From: A novel inverse membrane bioreactor for efficient bioconversion from methane gas to liquid methanol using a microbial gas-phase reaction

Fig. 7

a Schematic of the continuous operation for the bioconversion of CH4 to CH3OH in the IMBR. b Effects of the gas flow rate on the consumption rate and consumption ratio of CH4. c Time courses of concentrations of CH4 and CH3OH at the outlet of the IMBR at 0.2 mL min−1 of the gas flow rate and 4 mL h−1 of the liquid flow rate. d Time courses of the consumption ratio of CH4 and CH3OH productivity in the IMBR

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