MgAl2O4 Spinel-Stabilized Calcium Oxide Absorbents with Improved Durability for High-Temperature CO2 Capture

被引:75
作者
Li, Liyu [1 ]
King, David L. [1 ]
Nie, Zimin [1 ]
Li, Xiaohong Shari [1 ]
Howard, Chris [1 ]
机构
[1] Pacific NW Natl Lab, Inst Interfacial Catalysis, Richland, WA 99354 USA
关键词
WARM GAS TEMPERATURES; CARBON-DIOXIDE; POWER-PLANT; FLUE-GAS; SORBENTS; CAO; CAPACITY; CYCLES; SORPTION; EFFICIENCY;
D O I
10.1021/ef100245q
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
With efficient energy recovery, calcium-oxide-based absorbents that operate at elevated temperatures have an advantage over absorbents that operate at lower temperatures for CO2 capture from coal power plants. The major limitation of these absorbents is that the carbonation and decarbonation reactions of CaO and CaCO3 are for from complete or reversible. Rapid loss of CO2 capacity over many carbonation/decarbonation cycles is always observed because of severe absorbent sintering. We have found that this sintering effect can be effectively mitigated by properly mixing calcium oxide precursors with small rod-like MgAl2O4 spinel nanoparticles. A new class of CaO-based absorbents with much improved high-temperature durability was developed by wet physical mixing of calcium acetate with nano MgAl2O4 spinet particles followed by high-temperature calcination. CaO-MgAl2O4 (32 wt % spinet content) material provides 34 wt % CO2 capacity after 65 carbonation decarbonation cycles (650 and 850 degrees C, respectively), corresponding to 63% CaO use. Under the same test conditions, the CO2 capacity of natural dolomite (35 wt % MgO and 65 wt % CaO) decreases rapidly from 25 wt % for the 1st cycle to less than 5 wt % for the 50th cycle.
引用
收藏
页码:3698 / 3703
页数:6
相关论文
共 42 条
[1]   Cost structure of a postcombustion CO2 capture system using CaO [J].
Abanades, J. Carlos ;
Grasa, G. ;
Alonso, M. ;
Rodriguez, N. ;
Anthony, E. J. ;
Romeo, L. M. .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2007, 41 (15) :5523-5527
[2]   Sorbent cost and performance in CO2 capture systems [J].
Abanades, JC ;
Rubin, ES ;
Anthony, EJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (13) :3462-3466
[3]   Fluidized bed combustion systems integrating CO2 capture with CaO [J].
Abanades, JC ;
Anthony, EJ ;
Wang, JS ;
Oakey, JE .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2005, 39 (08) :2861-2866
[4]   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
[5]   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
[6]  
[Anonymous], THESIS U WATERLOO WA
[7]  
[Anonymous], 2016, CARBON DIOXIDE CAPTU
[8]  
[Anonymous], 2008, Patent No. [US731484781, 7314847]
[9]  
BARKER R, 1973, J APPL CHEM BIOTECHN, V23, P733
[10]   The calcium looping cycle for large-scale CO2 capture [J].
Blamey, J. ;
Anthony, E. J. ;
Wang, J. ;
Fennell, P. S. .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2010, 36 (02) :260-279