The maximum capture efficiency of CO2 using a carbonation/calcination cycle of CaO/CaCO3

被引:537
作者
Abanades, JC [1 ]
机构
[1] CSIC, Inst Carboquim, Dept Energy & Environm, Zaragoza 50015, Spain
关键词
CO2; capture; separation; carbonation; calcination;
D O I
10.1016/S1385-8947(02)00126-2
中图分类号
X [环境科学、安全科学];
学科分类号
08 [工学]; 0830 [环境科学与工程];
摘要
The use of natural calcium carbonates as regenerable CO2 sorbents in industrial processes is limited by the rapid decay of the carbonation conversion with the number of cycles carbonation/calcination. However, new processes are emerging to capture CO2 using these cycles, that can take advantage of the intrinsic benefits of high temperature separations in energy systems. This work presents an analysis of a general carbonation/calcination cycle to capture CO2, incorporating a fresh feed of sorbent to compensate for the decay in activity during sorbent re-cycling. A general design equation for the maximum CO2 capture efficiency is obtained by incorporating to the cycle mass balances a simple but realistic equation to estimate the decay in sorbent activity with the number of cycles. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:303 / 306
页数:4
相关论文
共 15 条
[1]
Development of porous solid reactant for thermal-energy storage and temperature upgrade using carbonation/decarbonation reaction [J].
Aihara, M ;
Nagai, T ;
Matsushita, J ;
Negishi, Y ;
Ohya, H .
APPLIED ENERGY, 2001, 69 (03) :225-238
[2]
[Anonymous], [No title captured], Patent No. 4191538
[3]
Hydrogen from methane in a single-step process [J].
Balasubramanian, B ;
Ortiz, AL ;
Kaytakoglu, S ;
Harrison, DP .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (15-16) :3543-3552
[4]
BARKER R, 1973, J APPL CHEM BIOTECHN, V23, P733
[5]
EFFECT OF THE PRODUCT LAYER ON THE KINETICS OF THE CO2-LIME REACTION [J].
BHATIA, SK ;
PERLMUTTER, DD .
AICHE JOURNAL, 1983, 29 (01) :79-86
[6]
CURRAN GP, 1967, ADV CHEM SER, P141
[7]
Capturing greenhouse gases [J].
Herzog, H ;
Eliasson, B ;
Kaarstad, O .
SCIENTIFIC AMERICAN, 2000, 282 (02) :72-79
[8]
What future for carbon capture and sequestration? [J].
Herzog, H .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2001, 35 (07) :148A-153A
[9]
Calcium oxide/carbon dioxide reactivity in a packed bed reactor of a chemical heat pump for high-temperature gas reactors [J].
Kato, Y ;
Yamada, M ;
Kanie, T ;
Yoshizawa, Y .
NUCLEAR ENGINEERING AND DESIGN, 2001, 210 (1-3) :1-8
[10]
LIN S, 1999, P ADV CLEAN COAL TEC, P1