2017
DOI: 10.1016/j.jcou.2017.10.010
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Modelling of equilibrium working capacity of PSA, TSA and TVSA processes for CO 2 adsorption under direct air capture conditions

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Cited by 104 publications
(68 citation statements)
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“…Thes orbent demonstrated remarkable stability over 40 consecutive sorption/desorption cycles,with acyclic CO 2 capture capacity of 0.8 mmol/g under dry conditions and apressure in the regeneration chamber of 200 mbar.Inthe combined TVS cycle,more than 90 % of the required energy input can be supplied as heat (< 100 8 8C), which could be derived from waste heat or solar thermal sources.W urzbacher et al pointed out that combining air capture with the solar-driven splitting of CO 2 offers ac losed-material cycle for producing synthetic liquid hydrocarbon fuels. [228] Elfving et al [229] modeled the equilibrium working capacity (EWC) of pressure-swing adsorption (PSA), temperature-swing adsorption (TSA), and temperature-vacuum swing adsorption (TVSA) processes for CO 2 sorption under DACc onditions.F or PSA, EWC values greater than 0.5 mmol CO 2 /g sorbent could not be achieved without exceeding reasonable boundaries for the vacuum pressure.I nc ontrast, with TSA and TVSA, EWC values greater than 0.7 mmol CO 2 /g sorbent could be reached under either dry and cold or warm and humid ambient conditions during CO 2 sorption at 400 ppm. Lively and Realff [230] presented athermodynamic analysis of the adsorption processes in the TSA and PSA modes during dilute gas separations and bulk gas separations.This study revealed that the TSA was more thermodynamically efficient at dilute concentrations of the adsorbate feed than bulk gas separations.C onversely,t he PSA system was more thermodynamically efficient for bulk gas separations.…”
Section: Class 2s Orbentsmentioning
confidence: 99%
“…Thes orbent demonstrated remarkable stability over 40 consecutive sorption/desorption cycles,with acyclic CO 2 capture capacity of 0.8 mmol/g under dry conditions and apressure in the regeneration chamber of 200 mbar.Inthe combined TVS cycle,more than 90 % of the required energy input can be supplied as heat (< 100 8 8C), which could be derived from waste heat or solar thermal sources.W urzbacher et al pointed out that combining air capture with the solar-driven splitting of CO 2 offers ac losed-material cycle for producing synthetic liquid hydrocarbon fuels. [228] Elfving et al [229] modeled the equilibrium working capacity (EWC) of pressure-swing adsorption (PSA), temperature-swing adsorption (TSA), and temperature-vacuum swing adsorption (TVSA) processes for CO 2 sorption under DACc onditions.F or PSA, EWC values greater than 0.5 mmol CO 2 /g sorbent could not be achieved without exceeding reasonable boundaries for the vacuum pressure.I nc ontrast, with TSA and TVSA, EWC values greater than 0.7 mmol CO 2 /g sorbent could be reached under either dry and cold or warm and humid ambient conditions during CO 2 sorption at 400 ppm. Lively and Realff [230] presented athermodynamic analysis of the adsorption processes in the TSA and PSA modes during dilute gas separations and bulk gas separations.This study revealed that the TSA was more thermodynamically efficient at dilute concentrations of the adsorbate feed than bulk gas separations.C onversely,t he PSA system was more thermodynamically efficient for bulk gas separations.…”
Section: Class 2s Orbentsmentioning
confidence: 99%
“…If there is moisture in the air and the air temperature is sufficient, liquid water is formed during the separation process. In humid conditions with a temperature of + 25°C, the molar ratio of separated H 2 O per CO 2 is 4.9 (Elfving et al 2017). If the separated water does not hold any harmful impurities, it can be used to replace fresh water consumed in production processes.…”
Section: Source Of Comentioning
confidence: 99%
“…wiesen darauf hin, dass die Kombination der Gewinnung aus der Luft mit der solarbetriebenen Spaltung von CO 2 einen geschlossenen Stoffkreislauf für die Herstellung von synthetischen flüssigen Kohlenwasserstoffbrennstoffen bietet . Elfving et al . modellierten die “Equilibrium Working Capacity” (EWC) der Vakuum‐Wechsel‐Adsorption (VSA), der Temperatur‐Wechsel‐Adsorption (TSA) und der Vakuum‐Druckwechsel‐Adsorption (TVSA) für die CO 2 ‐Sorption bei DAC‐Bedingungen.…”
Section: Sorbenten Zur Gewinnung Von Co2 Aus Der Umgebungsluftunclassified