2022
DOI: 10.1016/j.cej.2021.131981
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Electrowinning-coupled CO2 capture with energy-efficient absorbent regeneration: Towards practical application

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Cited by 39 publications
(19 citation statements)
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“…Carbon dioxide electrolyzers can produce carbon-neutral chemicals and fuels using CO 2 from the atmosphere and electricity from wind and solar resources. To be industrially relevant, CO 2 electrolyzers must achieve high rates of product formation (i.e., current densities >100 mA cm –2 ) and low cell potentials (<3 V) while also efficiently utilizing the CO 2 reactant. , Gaseous CO 2 is often used as the feedstock for pilot-scale CO 2 electrolyzers because of its solubility and mass transfer advantages over CO 2 dissolved in water. However, isolating pure CO 2 gas from point sources or the atmosphere is costly because a considerable energy penalty (i.e., 50–175 kJ mol –1 of CO 2 ) is required to liberate CO 2 from liquid sorbents used in CO 2 capture processes. These collected CO 2 streams are also not often utilized efficiently in gas-fed CO 2 electrolyzers, since a major fraction of the reacted CO 2 is converted into HCO 3 – and CO 3 2– (referred to here as (bi)­carbonates) upon reacting with OH – produced at the cathode . These (bi)­carbonates are inevitably converted back into CO 2 at the anode .…”
mentioning
confidence: 99%
“…Carbon dioxide electrolyzers can produce carbon-neutral chemicals and fuels using CO 2 from the atmosphere and electricity from wind and solar resources. To be industrially relevant, CO 2 electrolyzers must achieve high rates of product formation (i.e., current densities >100 mA cm –2 ) and low cell potentials (<3 V) while also efficiently utilizing the CO 2 reactant. , Gaseous CO 2 is often used as the feedstock for pilot-scale CO 2 electrolyzers because of its solubility and mass transfer advantages over CO 2 dissolved in water. However, isolating pure CO 2 gas from point sources or the atmosphere is costly because a considerable energy penalty (i.e., 50–175 kJ mol –1 of CO 2 ) is required to liberate CO 2 from liquid sorbents used in CO 2 capture processes. These collected CO 2 streams are also not often utilized efficiently in gas-fed CO 2 electrolyzers, since a major fraction of the reacted CO 2 is converted into HCO 3 – and CO 3 2– (referred to here as (bi)­carbonates) upon reacting with OH – produced at the cathode . These (bi)­carbonates are inevitably converted back into CO 2 at the anode .…”
mentioning
confidence: 99%
“…Investigations on the replenishment mechanism of the electrolyte and additives as well as economic estimations of the cost input and output return for crude Pb electrorefining in the Lugalvan BNO12-assisted MSA system are now being performed. The energetic performance and process design of electrorefining would be further improved by low-investment microkinetic modeling. Preparation of novel electrodes with nano- and polymeric materials will further improve the electrochemical performance of the deposition process. The continuous drop in price of renewable electricity would further advance electrorefining toward lower-cost operation. Overall, crude Pb electrorefining in the Lugalvan BNO12-assisted MSA system would operate in a more technically and economically beneficial mode once receiving reasonable optimizations of process and condition and hold great potential toward practical application.…”
Section: Discussionmentioning
confidence: 99%
“…, α 0 and ß 0 based on the Tafel law (details in Supporting Information, Section S1 and Figure S4). The modeled energy consumption (W m ) was estimated through the following equation: [16,27] W m ½kJ e mol HfðOEtÞ 4…”
Section: Microkinetic Modelingmentioning
confidence: 99%
“…[10] These are because the electrochemical process acts directly on the target substance, but not the medium. [16] For example, aluminium, despite being the largest distributed metal in the earth's crust, was equal in value to silver before the wide deployment of the electrochemical Hall-Herold method. [17] Furthermore, no consumable items like expensive ion exchange membranes is needed for dividing the anode and cathode because of the synergistically combined redox transformations on the anode and cathode of EHS.…”
Section: Introductionmentioning
confidence: 99%