Abstract
A microchannel electrochemical reactor system was designed to facilitate the reduction of CO2 to CO, which is composed of a premixing section in the upstream consisting of a circular microchannel for the presaturation of CO2 in the electrolyte and a reacting section in the downstream consisting of an annular microchannel containing a Ag rod as the catalyst. Such a combined structure exhibited an ultrahigh CO faradaic efficiency of 95.3% due to the efficient mass transfer under Taylor flow. It is interesting to find that CO2 conversion was increased from 0.94 to 3.66% when the length of the microchannel was increased by connection in series due to the prolonged contacting time between CO2 and the electrocatalyst. Furthermore, "scale-up" experiments demonstrated that the faradaic efficiency for CO could keep all above 95.0% at a current density of 7.5
Original language | English |
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Pages (from-to) | 5664-5674 |
Number of pages | 11 |
Journal | Industrial and Engineering Chemistry Research |
Volume | 59 |
Issue number | 13 |
DOIs | |
State | Published - 1 Apr 2020 |
Externally published | Yes |
Bibliographical note
Publisher Copyright:Copyright © 2020 American Chemical Society.
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
- Industrial and Manufacturing Engineering