Please use this identifier to cite or link to this item: http://hdl.handle.net/11455/68994
標題: Thermodynamics and regeneration of CO2 adsorption on mesoporous spherical-silica particles
作者: Lu, C.Y.
Su, F.S.
Hsu, S.C.
Chen, W.F.
Bai, H.L.
Hwang, J.F.
Lee, H.H.
關鍵字: Mesoporous spherical-silica particles;CO2 capture;Isosteric heat of;adsorption;Cyclic CO2 adsorption;walled carbon nanotubes;molecular-sieve mcm-41;greenhouse-gas;activated carbon;organic vapors;natural-gas;flue-gas;capture;separation;sorbents
Project: Fuel Processing Technology
期刊/報告no:: Fuel Processing Technology, Volume 90, Issue 12, Page(s) 1543-1549.
摘要: 
Mesoporous spherical-silica particles (MSPs) were modified by N-[3-(trimethoxysilyl) propyllethylenediamine (EDA) solution and were employed as sorbents to study thermodynamics and regeneration Of CO2 adsorption from gas streams. The thermodynamic analysis gave low isosteric heats of adsorption, which are typical for physical adsorption. The cyclic CO2 adsorption on MSP(EDA) showed that the adsorbed CO2 could be effectively desorbed via thermal treatment at 120 degrees C for 25 min while the adsorbed CO2 due to physical interaction could be effectively desorbed via vacuum suction at 0.145 bar for 30 min. If a combination of thermal treatment and vacuum suction was conducted at 120 degrees C and 0.145 bar, the time for effectively desorbing CO2 could be shortened to 7.5 min and thus reduces a significant amount of energy penalty. The adsorption capacities and the physicochemical properties of MSP(EDA) were preserved after 15 cycles of adsorption and regeneration. These results suggest that the MSP(EDA) can be stably employed in the prolonged cyclic adsorption and that they are thus possibly cost-effective sorbents for CO2 capture from flue gases. (C) 2009 Elsevier B.V. All rights reserved.
URI: http://hdl.handle.net/11455/68994
ISSN: 0378-3820
DOI: 10.1016/j.fuproc.2009.08.002
Appears in Collections:期刊論文

Show full item record
 

Google ScholarTM

Check

Altmetric

Altmetric


Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.