Magnesia-Stabilized Calcium Oxide Absorbents with Improved Durability for High Temperature CO2 Capture

被引:169
作者
Li, Liyu [1 ]
King, David L. [1 ]
Nie, Zimin [1 ]
Howard, Chris [1 ]
机构
[1] Pacific NW Natl Lab, Inst Interfacial Catalysis, Richland, WA 99354 USA
关键词
CARBON-DIOXIDE; HYDROGEN-PRODUCTION; CAPACITY; SORBENTS; SORPTION; CAO; EFFICIENCY; STORAGE; CYCLES;
D O I
10.1021/ie901166b
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Calcium oxide based materials are attractive regenerable absorbents for separating CO2 from hot gas streams because of their high reactivity, high CO2 capacity, and low material cost. Their high carbonation temperature makes it possible to recover and use high quality heat released during CO2 capture, which increases overall process efficiency. However, the performance of all reported CaO-based absorbents deteriorates as the number of carbonation-decarbonation cycles increases. This is caused by absorbent sintering during the highly exothermic carbonation process. We have found that sintering can be effectively mitigated by properly mixing with a modest amount of MgO. A class of CaO-based absorbents with improved durability and CO2 reactivity were prepared by physical mixing of Ca(CH3COO)(2) with small MgO particles followed by high temperature calcination. With 26 wt % MgO content, a CaO-MgO mixture prepared by this method gives as high as 53 wt % CO2 capacity after 50 carbonation-decarbonation cycles at 758 degrees C. Without MgO addition, the CO2 capacity of pure CaO obtained from the same source decreases from 66 wt % for the first cycle to 26 wt % for the 50th cycle under the same test conditions.
引用
收藏
页码:10604 / 10613
页数:10
相关论文
共 23 条
[1]   Sorbent cost and performance in CO2 capture systems [J].
Abanades, JC ;
Rubin, ES ;
Anthony, EJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (13) :3462-3466
[2]   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
[3]   Development of a CaO-Based CO2 Sorbent with Improved Cyclic Stability [J].
Albrecht, Karl O. ;
Wagenbach, Kyle S. ;
Satrio, Justinus A. ;
Shanks, Brent H. ;
Wheelock, Thomas D. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (20) :7841-7848
[4]  
FAN LS, 2006, Patent No. 7067456
[5]   Overcoming the problem of loss-in-capacity of calcium oxide in CO2 capture [J].
Feng, Bo ;
Liu, Wenqiang ;
Li, Xiang ;
An, Hui .
ENERGY & FUELS, 2006, 20 (06) :2417-2420
[6]   Enhanced hydrogen production from biomass with in situ carbon dioxide capture using calcium oxide sorbents [J].
Florin, Nicholas H. ;
Harris, Andrew T. .
CHEMICAL ENGINEERING SCIENCE, 2008, 63 (02) :287-316
[7]   CO2 capture capacity of CaO in long series of carbonation/calcination cycles [J].
Grasa, Gemma S. ;
Abanades, J. Carlos .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (26) :8846-8851
[8]   Carbonation-calcination cycle using high reactivity calcium oxide for carbon dioxide separation from flue gas [J].
Gupta, H ;
Fan, LS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (16) :4035-4042
[9]   Multicyclic study on the simultaneous carbonation and sulfation of high-reactivity CaO [J].
Iyer, MV ;
Gupta, H ;
Sakadjian, BB ;
Fan, LS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (14) :3939-3947
[10]   Novel CO2 absorbents using lithium-containing oxide [J].
Kato, M ;
Nakagawa, K ;
Essaki, K ;
Maezawa, Y ;
Takeda, S ;
Kogo, R ;
Hagiwara, Y .
INTERNATIONAL JOURNAL OF APPLIED CERAMIC TECHNOLOGY, 2005, 2 (06) :467-475