Chilled ammonia process for CO2 capture

被引:133
作者
Darde, Victor [1 ,2 ]
Thomsen, Kaj [1 ]
van Well, Willy J. M. [2 ]
Stenby, Erling H. [1 ]
机构
[1] Tech Univ Denmark, Bldg 229, DK-2800 Lyngby, Denmark
[2] DONG EnergyPower, Chem Engn, DK-7000 Frederiksberg, Denmark
来源
GREENHOUSE GAS CONTROL TECHNOLOGIES 9 | 2009年 / 1卷 / 01期
关键词
CO2; capture; Chilled ammonia process; Extended UNIQUAC model; Aqueous ammonia; Carbon dioxide; NH3; H2O; AQUEOUS-SOLUTIONS; MONOETHANOLAMINE; DEGRADATION; SYSTEMS; BLENDS;
D O I
10.1016/j.egypro.2009.01.137
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
The chilled ammonia process absorbs the CO2 at low temperature (2-10 degrees C). The heat of absorption of carbon dioxide by ammonia is significantly lower than for amines. In addition, degradation problems can be avoided and a high carbon dioxide capacity is achieved. Hence, this process shows good perspectives for decreasing the energy requirement. However, a scientific understanding of the processes is required. The properties of the NH3-CO2-H2O system were described using the Extended UNIQUAC electrolyte model developed by Thomsen and Rasmussen in a temperature range from 0 to 110 degrees C and pressure up to 100 bars [1]. The results show that solid phases consisting of ammonium carbonate and bicarbonate are formed in the absorber. The energy requirements in the absorber and in the desorber have been studied. The enthalpy calculations show that an energy requirement for the desorber lower than 2 GJ/ton CO2 can be reached. (c) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1035 / 1042
页数:8
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