TY - GEN
T1 - Adsorptive filtration of carbon dioxide from wet gases utilizing microfibrous filter media entrapped K2CO3
AU - Sathitsuksanoh, Noppadon
AU - Yang, Hongyun
AU - Cahela, Donald R.
AU - Lu, Yong
AU - Tatarchuk, Bruce J.
PY - 2005
Y1 - 2005
N2 - Present commercial CO2 removal units utilize a physical solvent of alkanolamine, such as MEA, diethanolamine, and methyldiethanolamine. A microfibrous entrapped sorbent was developed for CO2 removal from flue gas. A microfibrous carrier consisting of 4 and 8 μm (dia) metal fibers was utilized to entrap 150-250 μm (dia) activated carbon particulates (ACP). K2CO3 was then loaded onto the support by pseudo-incipient wetness at various loadings by varying the solution concentration. The adsorption capacity of CO2 at various K2CO3 loadings was studied. The nano-dispersed nature of K2CO3 combined with the use of small support particulates promoted high K2CO3 utilization, high contacting efficiency, and high accessibility of K2CO3. At equivalent bed volumes, K2CO3/ACP entrapped materials provided longer breakthrough times for CO2 removal compared to packed beds of K2CO3 pellets. At 87% relative humidity, maximum capacity at room temperature based on total weight of adsorbents was ∼ 0.037 g CO2 with optimal loading of 30 wt % K2CO3 for packed beds corresponding to 33% utilization of impregnated K2CO3. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).
AB - Present commercial CO2 removal units utilize a physical solvent of alkanolamine, such as MEA, diethanolamine, and methyldiethanolamine. A microfibrous entrapped sorbent was developed for CO2 removal from flue gas. A microfibrous carrier consisting of 4 and 8 μm (dia) metal fibers was utilized to entrap 150-250 μm (dia) activated carbon particulates (ACP). K2CO3 was then loaded onto the support by pseudo-incipient wetness at various loadings by varying the solution concentration. The adsorption capacity of CO2 at various K2CO3 loadings was studied. The nano-dispersed nature of K2CO3 combined with the use of small support particulates promoted high K2CO3 utilization, high contacting efficiency, and high accessibility of K2CO3. At equivalent bed volumes, K2CO3/ACP entrapped materials provided longer breakthrough times for CO2 removal compared to packed beds of K2CO3 pellets. At 87% relative humidity, maximum capacity at room temperature based on total weight of adsorbents was ∼ 0.037 g CO2 with optimal loading of 30 wt % K2CO3 for packed beds corresponding to 33% utilization of impregnated K2CO3. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).
UR - https://www.scopus.com/pages/publications/84916886090
M3 - 会议稿件
AN - SCOPUS:84916886090
SN - 0816909962
SN - 9780816909964
T3 - AIChE Annual Meeting Conference Proceedings
BT - 05AIChE
PB - American Institute of Chemical Engineers
T2 - 05AIChE: 2005 AIChE Annual Meeting and Fall Showcase
Y2 - 30 October 2005 through 4 November 2005
ER -