Effect of the Carbonation Temperature on the CO2 Carrying Capacity of CaO

被引:70
作者
Criado, Yolanda A. [1 ]
Arias, Borja [1 ]
Carlos Abanades, J. [1 ]
机构
[1] CSIC, INCAR, C Francisco Pintado Fe 26, Oviedo 33011, Spain
关键词
PRODUCT LAYER; CAPTURE SYSTEM; CALCIUM-OXIDE; SORBENTS; KINETICS;
D O I
10.1021/acs.iecr.8b02111
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The calcium looping process based on the CaO/CaCO3 carbonation/calcination cycle has been proven to be an efficient CO2 capture technology. Most of the experimental work describing the behavior of the CaO particles has been performed under carbonation reference conditions of 650 degrees C and 10-15% vol CO2. Although, process schemes recently proposed have pointed out the practical benefits of operating the carbonator reactor at lower temperatures, on the assumption that these would lead to higher CO2 capture efficiencies. However, there is a lack of correlations for estimating the evolution of the carrying capacity along cycling at temperatures below 650 degrees C. Therefore, in this work the carrying capacity of a high purity natural Ca-material used as reference has been studied in a selected range of representative carbonation temperatures (450-725 degrees C). The parameters on the CaO deactivation curve that is widely employed have been readjusted to accord with a more general decay model that takes into account the effect of the carbonation temperature on the thickness of the CaCO3 product layer that marks the end of the fast kinetically controlled regime.
引用
收藏
页码:12595 / 12599
页数:5
相关论文
共 31 条
[11]   CaCO3 Crystallite Evolution during CaO Carbonation: Critical Crystallite Size and Rate Constant Measurement by In-Situ Synchrotron Radiation X-ray Powder Diffraction [J].
Biasin, A. ;
Segre, C. U. ;
Strumendo, M. .
CRYSTAL GROWTH & DESIGN, 2015, 15 (11) :5188-5201
[12]   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
[13]   Calcium looping CO2 capture system for back-up power plants [J].
Criado, Y. A. ;
Arias, B. ;
Abanades, J. C. .
ENERGY & ENVIRONMENTAL SCIENCE, 2017, 10 (09) :1994-2004
[14]   Kinetics of the CaO/Ca(OH)2 Hydration/Dehydration Reaction for Thermochemical Energy Storage Applications [J].
Criado, Yolanda A. ;
Alonso, Monica ;
Abanades, J. Carlos .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (32) :12594-12601
[15]   Calcium looping sorbents for CO2 capture [J].
Erans, Maria ;
Manovic, Vasilije ;
Anthony, Edward J. .
APPLIED ENERGY, 2016, 180 :722-742
[16]   Application of the Random Pore Model to the Carbonation Cyclic Reaction [J].
Grasa, Gemma ;
Murillo, Ramon ;
Alonso, Monica ;
Abanades, J. Carlos .
AICHE JOURNAL, 2009, 55 (05) :1246-1255
[17]   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
[18]  
Intergovernmental Panel on Climate Change, 2014, IPCC CLIM CHANG 2014
[19]   CaO-Based CO2 Sorbents: From Fundamentals to the Development of New, Highly Effective Materials [J].
Kierzkowska, Agnieszka M. ;
Pacciani, Roberta ;
Mueller, Christoph R. .
CHEMSUSCHEM, 2013, 6 (07) :1130-1148
[20]   Effect of Temperature on the Carbonation Reaction of CaO with CO2 [J].
Li, Zhen-shan ;
Fang, Fan ;
Tang, Xiao-yu ;
Cai, Ning-sheng .
ENERGY & FUELS, 2012, 26 (04) :2473-2482