Microbial electrosynthesis (MES) is a promising carbon utilization technology, but the low-value products (i.e., acetate or methane) and the high electric power demand hinder its industrial adoption. In this study, electrically efficient MES cells with a low ohmic resistance of 15.7 mΩ m were operated galvanostatically in fed-batch mode, alternating periods of high CO and H availability. This promoted acetic acid and ethanol production, ultimately triggering selective (78% on a carbon basis) butyric acid production via chain elongation. An average production rate of 14.5 g m d was obtained at an applied current of 1.0 or 1.5 mA cm, being sp. the key chain elongating player. Inoculating a second cell with the catholyte containing the enriched community resulted in butyric acid production at the same rate as the previous cell, but the lag phase was reduced by 82%. Furthermore, interrupting the CO feeding and setting a constant pH of 1.7-1.8 atm in the cathode compartment triggered solventogenic butanol production at a pH below 4.8. The efficient cell design resulted in average cell voltages of 2.6-2.8 V and a remarkably low electric energy requirement of 34.6 kWh kg of butyric acid produced, despite coulombic efficiencies being restricted to 45% due to the cross-over of O and H through the membrane. In conclusion, this study revealed the optimal operating conditions to achieve energy-efficient butyric acid production from CO and suggested a strategy to further upgrade it to valuable butanol.
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http://www.ncbi.nlm.nih.gov/pmc/articles/PMC10457423 | PMC |
http://dx.doi.org/10.1016/j.ese.2023.100303 | DOI Listing |
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