2022
DOI: 10.1016/j.jece.2022.108759
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Performance of TSA and VSA post-combustion CO2 capture processes with a biomass waste-based adsorbent

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Cited by 18 publications
(4 citation statements)
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“…Secondly, waste heat can be used to provide the energy that is needed for temperature swing. Therefore, the low temperature difference between the regeneration and adsorption steps of TSA (30-150 • C) and the possibility to use the available waste heat reduce the operating cost, thereby promoting the implementation of TSA [46]. Nowadays, TSA is mainly employed for post-combustion capture of CO 2 from flue gases [47].…”
Section: Adsorptionmentioning
confidence: 99%
“…Secondly, waste heat can be used to provide the energy that is needed for temperature swing. Therefore, the low temperature difference between the regeneration and adsorption steps of TSA (30-150 • C) and the possibility to use the available waste heat reduce the operating cost, thereby promoting the implementation of TSA [46]. Nowadays, TSA is mainly employed for post-combustion capture of CO 2 from flue gases [47].…”
Section: Adsorptionmentioning
confidence: 99%
“…Reprinted with permission of AIP Conference Proceedings from Tomas et al (2017) TSA techniques are often devoid of noise and vibration, but they typically involve adsorbents with sluggish conductivity, and the adsorption (cooling) and desorption (heating) cycle periods are rather lengthy (Akdag et al 2022, Gutierrez-Ortega et al 2022. Hence, hoover pressure may help regeneration.…”
Section: Acmentioning
confidence: 99%
“…The capture of greenhouse gases, such as CO2, from dilute sources (e.g. flue gas which generally contains 4 -30 % CO2 in a mixture with N2) [3] has generally been achieved at an industrial scale using alkanoamines such as monoethanolamine (MEA) [4]. However, the chemical instability, their corrosiveness, and the cost of many alkanoamines limit their widespread application.…”
Section: Introductionmentioning
confidence: 99%
“…In contrast, adsorption-based processes for the capture and separation of CO2 using porous sorbents have been proposed as a promising energy-and cost-efficient alternative. Pressure-vacuum-and temperature-swing (PSVA, and TSA) adsorption have been explored at both lab-and pilot scales to successfully drive the capture and regeneration of CO2 in sorbents such as zeolites [6][7][8][9], porous carbons [3,10], and metal-organic frameworks (MOFs) /porous coordination polymers (PCPs) [11][12][13]. Although the running costs of such processes using porous sorbents offer significant benefits as compared to CO2 capture using amine compounds, problems with these techniques still exist and are related to e.g.…”
Section: Introductionmentioning
confidence: 99%