2023
DOI: 10.1021/acs.iecr.3c02183
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Unraveling the Potential of Electrochemical pH-Swing Processes for Carbon Dioxide Capture and Utilization

Thanh Ngoc-Dan Cao,
Seth W Snyder,
Yu-I Lin
et al.
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Cited by 5 publications
(4 citation statements)
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“…Ideal cycle energy is found to be as low as around 250 kJ/mol for certain operating regimes, although it is expected that higher energy will be required if higher cycle capacity is desirable. For context, redox electrochemical DAC processes have been shown to reach 100 kJ/mol on bench scale systems, and industrial solid sorbent and calcium-looping processes can reach energy requirements lower than 300 kJ/mol . To reach similar or lower energy levels, energy recovery modules that recover energy from the salinity differences created through the NF and RO modules can significantly reduce the energy cost of capture.…”
Section: Resultsmentioning
confidence: 99%
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“…Ideal cycle energy is found to be as low as around 250 kJ/mol for certain operating regimes, although it is expected that higher energy will be required if higher cycle capacity is desirable. For context, redox electrochemical DAC processes have been shown to reach 100 kJ/mol on bench scale systems, and industrial solid sorbent and calcium-looping processes can reach energy requirements lower than 300 kJ/mol . To reach similar or lower energy levels, energy recovery modules that recover energy from the salinity differences created through the NF and RO modules can significantly reduce the energy cost of capture.…”
Section: Resultsmentioning
confidence: 99%
“…The NF selectivity results that we report in this work are also directly applicable to approaches beyond DAC and are useful for any method that seeks to control the relative concentration of DIC species in solution. In particular, recent studies have reported that bicarbonate-rich solution can be used as a feed for electrolytic conversion to useful chemicals. ,,, For example, Lees et al (2020) describe a process that captures CO 2 from the atmosphere or flue gas and uses electrolyzers to convert a 3 M KHCO3 solution into CO . However, the step between CO 2 absorption, which must happen at high pH conditions and therefore is dominated by carbonate ions, and the bicarbonate-rich end point is not explored.…”
Section: Resultsmentioning
confidence: 99%
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“…Subsequently, the excess acid is removed to regenerate the starting sorbent. This process is known as pH swing desorption and is typically achieved by dialysis or by modulating the pH using a spectator analyte. …”
mentioning
confidence: 99%