Influence of material composition on the CO2 and H2O adsorption capacities and kinetics of potassium-promoted sorbents

被引:24
作者
Coenen, Kai [1 ]
Gallucci, Fausto [1 ]
Cobden, Paul [2 ]
van Dijk, Eric [2 ]
Hensen, Emiel [1 ]
Annaland, Martin van Sint [1 ]
机构
[1] Eindhoven Univ Technol, Dept Chem Engn & Chem, POB 513, Eindhoven, Netherlands
[2] ECN, Sustainable Proc Technol, POB, NL-1755 ZG Petten, Netherlands
关键词
SEWGS; Cyclic working capacity; K2CO3; decomposition; WATER-GAS-SHIFT; HYDROTALCITE-LIKE COMPOUNDS; HIGH-TEMPERATURE; CARBON-DIOXIDE; DESORPTION BEHAVIOR; SORPTION; CAPTURE; CHEMISORPTION; SEWGS; BASICITY;
D O I
10.1016/j.cej.2017.11.161
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Two different potassium-promoted hydrotalcite (HTC)-based adsorbents and a potassium-promoted alumina sorbent were investigated using thermogravimetric analysis (TGA) and different characterization methods in order to study CO2 and H2O adsorption capacity and kinetics. A higher Mg content improves the cyclic working capacity for CO2 due to the higher basicity of the material. The initial adsorption rate for CO2 is very fast for all sorbents, but for sorbents with higher MgO content, this fast-initial adsorption is followed by a slower CO2 uptake probably caused by the slow formation of bulk carbonates. A longer half-cycle time can therefore increase the CO2 cyclic working capacity for sorbents with a higher MgO content. Potassium-promoted alumina has a very stable CO2 cyclic working capacity at different operating temperatures compared to the potassium-promoted HTC's. Usually a higher operating temperature increases the desorption kinetics for a HTC-based adsorbent, but not for potassium-promoted alumina. HTC-based adsorbents show the highest cyclic working capacity for H2O. The adsorption kinetics for H2O are not influenced by the material composition, indicating that the mechanism behind the adsorption of H2O is different compared to CO2. Depending on the material composition, adsorption of steam at high operating temperatures (>500 degrees C) results in an irreversible decomposition of carbonate species. Steam can reduce the temperature where usually K2CO3 is irreversibly decomposed resulting in a significantly reduced cyclic working capacity, which is very important concerning the use of these sorbents for sorption-enhanced water-gas shift processes.
引用
收藏
页码:2115 / 2123
页数:9
相关论文
共 29 条
[1]   Progress in hydrotalcite like compounds and metal-based oxides for CO2 capture: a review. [J].
Bhatta, Lakshminarayana Kudinalli Gopalakrishna ;
Subramanyam, Seetharamu ;
Chengala, Madhusoodana D. ;
Olivera, Sharon ;
Venkatesh, Krishna .
JOURNAL OF CLEANER PRODUCTION, 2015, 103 :171-196
[2]   Comparison of the efficiency of carbon dioxide capture by sorption-enhanced water-gas shift and palladium-based membranes for power and hydrogen production [J].
Boon, Jurriaan ;
Spallina, Vincenzo ;
van Delft, Yvonne ;
Annaland, Martin van Sint .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2016, 50 :121-134
[3]   Isotherm model for high-temperature, high-pressure adsorption of CO2 and H2O on K-promoted hydrotalcite [J].
Boon, Jurriaan ;
Cobden, P. D. ;
van Dijk, H. A. J. ;
Hoogland, C. ;
van Selow, E. R. ;
Annaland, M. van Sint .
CHEMICAL ENGINEERING JOURNAL, 2014, 248 :406-414
[4]   On the influence of steam on the CO2 chemisorption capacity of a hydrotalcite-based adsorbent for SEWGS applications [J].
Coenen, Kai ;
Gallucci, Fausto ;
Pio, Gianmaria ;
Cobden, Paul ;
van Dijk, Eric ;
Hensen, Emiel ;
Annaland, Martin van Sint .
CHEMICAL ENGINEERING JOURNAL, 2017, 314 :554-569
[5]   Chemisorption working capacity and kinetics of CO2 and H2O of hydrotalcite-based adsorbents for sorption-enhanced water-gas-shift applications [J].
Coenen, Kai ;
Gallucci, Fausto ;
Cobden, Paul ;
van Dijk, Eric ;
Hensen, Emiel ;
Annaland, Martin van Sint .
CHEMICAL ENGINEERING JOURNAL, 2016, 293 :9-23
[6]   Exploring, Tuning, and Exploiting the Basicity of Hydrotalcites for Applications in Heterogeneous Catalysis [J].
Debecker, Damien P. ;
Gaigneaux, Eric M. ;
Busca, Guido .
CHEMISTRY-A EUROPEAN JOURNAL, 2009, 15 (16) :3920-3935
[7]  
Dragicevic D., 2013, ENERGY PROCEDIA, V2013
[8]   Temperature Dependence of the Nonequilibrium Kinetic Model That Describes the Adsorption and Desorption Behavior of CO2 in K-Promoted HTlc [J].
Du, Hai ;
Ebner, Armin D. ;
Ritter, James A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (07) :3328-3336
[9]   Understanding the adsorption and desorption behavior of CO2 on a K-promoted hydrotalcite-like compound (HTlc) through nonequilibrium dynamic isotherms [J].
Ebner, Armin D. ;
Reynolds, Steven P. ;
Ritter, James A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (18) :6387-6392
[10]   CO2 capture in integrated gasification combined cycle with SEWGS - Part A: Thermodynamic performances [J].
Gazzani, Matteo ;
Macchi, Ennio ;
Manzolini, Giampaolo .
FUEL, 2013, 105 :206-219