Quantitative Evaluation of the Aqueous-Ammonia Process for CO2 Capture Using Fundamental Data and Thermodynamic Analysis

被引:29
作者
Mathias, Paul M. [1 ]
Reddy, Satish [1 ]
O'Connell, John P. [2 ]
机构
[1] Fluor Corp, 47 Discovery, Irvine, CA 92618 USA
[2] Univ Virginia, Dept Chem Engn, Charlottesville, VA 22904 USA
来源
GREENHOUSE GAS CONTROL TECHNOLOGIES 9 | 2009年 / 1卷 / 01期
关键词
post-combustion CO2 capture; thermodynamic analysis; process modeling; electrolytes; absorption; solution nonideality; speciation; alkanolamines; ammonia; heat of reaction; CARBON-DIOXIDE; EQUILIBRIA; ENTHALPY;
D O I
10.1016/j.egypro.2009.01.161
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
There is strong world-wide interest in developing new and improved processes for post-combustion capture of CO2, usually using chemical absorption. Developers of new processes make positive claims for their proposals in terms of low energy consumption, but these are usually difficult to validate. This paper demonstrates that rigorous application of thermodynamic analysis and process simulation provides a powerful way to quantitatively evaluate the energy requirements of CO2-capture processes by applying this methodology to the analysis of the chilled-ammonia process. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1227 / 1234
页数:8
相关论文
共 18 条
[1]   Separation of CO2 from flue gas:: A review [J].
Aaron, D ;
Tsouris, C .
SEPARATION SCIENCE AND TECHNOLOGY, 2005, 40 (1-3) :321-348
[2]   Post-combustion decarbonisation processes [J].
Bailey, DW ;
Feron, PHM .
OIL & GAS SCIENCE AND TECHNOLOGY-REVUE D IFP ENERGIES NOUVELLES, 2005, 60 (03) :461-474
[3]  
Carson JK, 2000, J CHEM THERMODYN, V32, P1285
[4]  
Chapel D., 1999, CAN SOC CHEM ENG ANN
[5]   LOCAL COMPOSITION MODEL FOR EXCESS GIBBS ENERGY OF ELECTROLYTE SYSTEMS .1. SINGLE SOLVENT, SINGLE COMPLETELY DISSOCIATED ELECTROLYTE SYSTEMS [J].
CHEN, CC ;
BRITT, HI ;
BOSTON, JF ;
EVANS, LB .
AICHE JOURNAL, 1982, 28 (04) :588-596
[6]  
Darde V, 2008, ICPWS 15 BERL SEPT 8
[7]  
DOE/NETL, 2007, DOENETL40102107
[8]  
Gal E., 2006, Patent, Patent No. [WO 2006022885, 2006022885, WO2006022885]
[9]   VAPOR LIQUID EQUILIBRIA IN AQUEOUS-SOLUTIONS OF AMMONIA AND CARBON-DIOXIDE AT TEMPERATURES BETWEEN 333-K AND 393-K AND PRESSURES UP TO 7 MPA [J].
GOPPERT, U ;
MAURER, G .
FLUID PHASE EQUILIBRIA, 1988, 41 (1-2) :153-185
[10]  
JANECKE E, 1929, Z FUER ELEKTROCHEMIE, V39, P332