Mass-transfer efficiency of a spray column for CO2 capture by MEA

被引：65

作者：

Kuntz, Jeffery ^{[1
]}

Aroonwilas, Adisorn ^{[1
]}

机构：

[1] Univ Regina, Fac Engn, Regina, SK S4S 0A2, Canada

来源：

GREENHOUSE GAS CONTROL TECHNOLOGIES 9 | 2009年 / 1卷 / 01期

关键词：

CO2; capture; absorption; spray column; mass transfer coefficient; mass transfer area; alkanolamine; ABSORPTION PERFORMANCE; STRUCTURED PACKINGS; PACKED-COLUMN; CONTACTORS;

D O I：

10.1016/j.egypro.2009.01.029

中图分类号：

TE [石油、天然气工业]; TK [能源与动力工程];

学科分类号：

0807 ; 0820 ;

摘要：

A parametric study of carbon dioxide (CO2) absorption performance into an aqueous solution of monoethanolamine (MEA) in the spray column was carried out experimentally over wide ranges of process conditions. The performance of the spray was interpreted in terms of the overall mass transfer coefficient (K(G)a(e)) and was found to vary with process parameters, including gas flow rate, liquid flow rate, CO2 partial pressure, MEA concentration, CO2 loading, and size of spray nozzle. The performance of the spray column was compared to that of a packed column and showed a promise for CO2 capture application. (C) 2008 Elsevier Ltd. All rights reserved

引用

页码：205 / 209

页数：5

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