A kinetic and process modeling study of CO2 capture with MEA-promoted potassium carbonate solutions
A kinetic and process modeling study of CO2 capture with MEA-promoted potassium carbonate solutions
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DOI:
10.1016/j.cej.2012.08.092
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发表时间:
2012-11
影响因子:
15.1
通讯作者:
Hendy Thee;Yohanes A. Suryaputradinata;K. Mumford;Kathryn H. Smith;G. Silva;S. Kentish;G. Stevens
中科院分区:
文献类型:
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作者:
Hendy Thee;Yohanes A. Suryaputradinata;K. Mumford;Kathryn H. Smith;G. Silva;S. Kentish;G. Stevens
Aqueous solutions of carbonate salts such as potassium carbonate (K2CO3) have gained widespread acceptance as viable solvents for pre and post combustion capture of carbon dioxide (CO2). However, due to poor reaction kinetics a rate promoter is considered essential to improve the rate of CO2absorption and hydration to bicarbonate. Using a well characterized wetted-wall column, we have evaluated the reaction kinetics of CO2absorption into a K2CO3solution promoted with monoethanolamine (MEA) under conditions resembling those found at industrial CO2capture plants. Results presented here show that at 63°C the addition of MEA in small quantities, 1.1M (5wt.%) and 2.2M (10wt.%), accelerates the overall rate of absorption of CO2in a 30wt.% potassium carbonate solvent by a factor of 16 and 45 respectively. The Arrhenius expression for the reaction between CO2and MEA is kMEA(M−1s−1)=4.24×109exp(−3825/T [K]) where the activation energy is 31.8kJmol−1. Incorporating our experimental results into Aspen Plus™, we have developed an E-NRTL model that can replicate pilot plant and simulate industrial capture processes employing K2CO3promoted with MEA as the capture agent.