SE-SR with sorbents based on calcium aluminates: Process optimization

被引:17
作者
Barelli, L. [1 ]
Bidini, G. [1 ]
Gallorini, F. [1 ]
机构
[1] Univ Perugia, Dept Engn, I-06125 Perugia, Italy
关键词
CaO-based sorbent; CO2; capture; SE-SR; Calcium aluminates; HYDROGEN-PRODUCTION; CO2; REMOVAL; CAPACITY; BEHAVIOR; CAPTURE;
D O I
10.1016/j.apenergy.2014.12.066
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
The development of a sustainable power generation using fossil fuels will be strongly encouraged in the future in order to achieve European targets in terms of CO2 emissions. In this context, sorption-enhanced steam reforming (SE-SR) is a promising process that can be implemented as a CCS pre-combustion methodology. Regarding conventional catalyst-CO2 sorbent materials, main challenges concern the development of innovative CO2 sorbents with higher stability and regeneration temperature lower than CaO one. In recent study, a high-performance material based on incorporation of CaO particles into calcium aluminates was developed by authors exhibiting high sorption capacity and stability in multi cycle process. In this study, such a sorbent was packed, together with the catalyst, in a fixed bed reactor and tested in multi-cycle SE-SR process optimizing the operating conditions. Sensitivity analysis was carried out in reference to feeding flow rate, steam to carbon molar ratio and material particle size. The innovative sorbent exhibits, in optimized process, significant performance improvements (in terms of H-2 purity and total CO2 amount adsorbed in each carbonation cycle) respect similar approaches available in the technical literature. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:110 / 118
页数:9
相关论文
共 26 条
[1]   Conversion limits in the reaction of CO2 with lime [J].
Abanades, JC ;
Alvarez, D .
ENERGY & FUELS, 2003, 17 (02) :308-315
[2]   Hydrogen production through sorption-enhanced steam methane reforming and membrane technology: A review [J].
Barelli, L. ;
Bidini, G. ;
Gallorini, F. ;
Servili, S. .
ENERGY, 2008, 33 (04) :554-570
[3]   Production of hydrogen through the carbonation-calcination reaction applied to CH4/CO2 mixtures [J].
Barelli, L. ;
Bidini, G. ;
Corradetti, A. ;
Desideri, U. .
ENERGY, 2007, 32 (05) :834-843
[4]   Study of the carbonation-calcination reaction applied to the hydrogen production from syngas [J].
Barelli, L. ;
Bidini, G. ;
Corradetti, A. ;
Desideri, U. .
ENERGY, 2007, 32 (05) :697-710
[5]   Synthesis and test of sorbents based on calcium aluminates for SE-SR [J].
Barelli, L. ;
Bidini, G. ;
Di Michele, A. ;
Gallorini, F. ;
Petrillo, C. ;
Sacchetti, F. .
APPLIED ENERGY, 2014, 127 :81-92
[6]   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
[7]   Adsorbent Materials for Carbon Dioxide Capture from Large Anthropogenic Point Sources [J].
Choi, Sunho ;
Drese, Jeffrey H. ;
Jones, Christopher W. .
CHEMSUSCHEM, 2009, 2 (09) :796-854
[8]   Materials challenges for the development of solid sorbents for post-combustion carbon capture [J].
Drage, Trevor C. ;
Snape, Colin E. ;
Stevens, Lee A. ;
Wood, Joseph ;
Wang, Jiawei ;
Cooper, Andrew I. ;
Dawson, Robert ;
Guo, Xiao ;
Satterley, Christopher ;
Irons, Robin .
JOURNAL OF MATERIALS CHEMISTRY, 2012, 22 (07) :2815-2823
[9]   Nonequilibrium kinetic model that describes the reversible adsorption and desorption behavior of CO2 in a K-promoted hydrotalcite-like compound [J].
Ebner, Armin D. ;
Reynolds, Steven P. ;
Ritter, James A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (06) :1737-1744
[10]   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