Mass-transfer studies of solid-base catalyst-aided CO_(2) absorption and solid-acid catalyst-aided CO_(2) desorption for CO_(2) capture in a pilot plant using aqueous solutions of MEA and blends of MEA-MDEA and BEA-AMP  

作　　者：James Coker Daniel Boafo Afari Jessica Narku-Tetteh Raphael Idem 

机构地区：[1]Clean Energy Technologies Research Institute(CETRI),University of Regina,3737 Wascana Parkway,Regina,SK S4S 0A2,Canada

出　　处：《Clean Energy》2019年第4期263-277,共15页清洁能源（英文）

摘　　要：Mass-transfer studies of catalyst-aided CO_(2) absorption and desorption were performed in a full-cycle,bench-scale pilot plant to improve CO_(2) absorption using 5M MEA,5M MEA-2M MDEA and 2M BEA-2M AMP.A solid-base catalyst,K/MgO,and an acid catalyst,HZSM-5,were used to facilitate absorption and desorption,respectively.Absorption and desorption mass-transfer performance was presented in terms of the overall mass-transfer coefficient of the gas side(KGav)and liquid side(K_(L)a_(v)),respectively.For non-catalytic runs,the highest K_(G)a_(V) and K_(L)a_(V) were 0.086 Kmol m^(3).kPa.hr and 0.7851 hr for 2M BEA-2M AMP solvent.The results showed 38.7% KGav and 23.6% K_(L)a_(v) increase for 2M BEA-2M AMP with only HZSM-5 catalyst in desorber and a 95% K_(G)a_(V) and 45% K_(L)a_(V) increase for both K/MgO catalyst and HZSM-5 catalyst.This was attributed to the role of K/MgO in bonding loosely with CO_(2) and making it available for the amine reaction.

关 键 词：HZSM-5 K/MgO catalyst CO_(2)removal efficiency CO_(2)capture mass-transfer coefficients of absorber(KGaV)and desorber(K_(L)a_(V)) 

分 类 号：O64[理学—物理化学]