Enhancing the gas–liquid mass transfer during microbial electrosynthesis by the variation of CO2 flow rate

2021 ◽  
Vol 101 ◽  
pp. 50-58 ◽  
Author(s):  
Mélida del Pilar Anzola Rojas ◽  
Marcelo Zaiat ◽  
Ernesto Rafael González ◽  
Heleen De Wever ◽  
Deepak Pant
Catalysts ◽  
2020 ◽  
Vol 11 (1) ◽  
pp. 40
Author(s):  
Vasan Sivalingam ◽  
Vafa Ahmadi ◽  
Omodara Babafemi ◽  
Carlos Dinamarca

This study presents a series of experiments to test the integration of syngas fermentation into a single-cell microbial electrosynthesis (MES) process. Minimal gas–liquid mass transfer is the primary bottleneck in such gas-fermentation processes. Therefore, we hypothesized that MES integration could trigger the thermodynamic barrier, resulting in higher gas–liquid mass transfer and product-formation rates. The study was performed in three different phases as batch experiments. The first phase dealt with mixed-culture fermentation at 1 bar H2 headspace pressure. During the second phase, surface electrodes were integrated into the fermentation medium, and investigations were performed in open-circuit mode. In the third phase, the electrodes were poised with a voltage, and the second phase was extended in closed-circuit mode. Phase 2 demonstrated three times the gas consumption (1021 mmol) and 63% more production of acetic acid (60 mmol/L) than Phase 1. However, Phase 3 failed; at –0.8 V, acetic acid was oxidized to yield hydrogen gas in the headspace.


RSC Advances ◽  
2016 ◽  
Vol 6 (111) ◽  
pp. 109978-109982 ◽  
Author(s):  
Young-Kee Kim ◽  
Sung-Yeob Lee ◽  
Byung-Keun Oh

In an enzyme process using a gas substrate, the enhanced gas liquid mass transfer rate of the gas substrate by methyl-functionalized mesoporous nanoparticles could improve the productivity.


1988 ◽  
Vol 27 (7) ◽  
pp. 1246-1259 ◽  
Author(s):  
Pyare Lal ◽  
Satendra Kumar ◽  
Siddh N. Upadhyay ◽  
Yogendra D. Upadhya

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