Crystallographic transformation of limestone during calcination under CO2

被引:76
作者
Manuel Valverde, Jose [1 ]
Medina, Santiago [2 ]
机构
[1] Univ Seville, Fac Phys, E-41012 Seville, Spain
[2] Univ Seville, Xray Lab CITIUS, E-41012 Seville, Spain
关键词
DECOMPOSITION REACTIONS; CALCITE DECOMPOSITION; THERMAL-DECOMPOSITION; POSTCOMBUSTION CO2; CAPTURE; KINETICS; CARBONATOR; PRESSURE; SORBENTS; EQUATION;
D O I
10.1039/c5cp02715b
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The calcination reaction of limestone (CaCO3) to yield lime (CaO) is at the heart of many industrial applications as well as natural processes. In the recently emerged calcium-looping technology, CO2 capture is accomplished by the carbonation of CaO in a gas-solid reactor (carbonator). CaO is derived by the calcination of limestone in a calciner reactor under necessarily high CO2 partial pressure and high temperature. In situ X-ray diffraction (XRD) has been employed in this work to gain further insight into the crystallographic transformation that takes place during the calcination of limestone under CO2, at partial pressures (P) close to the equilibrium pressure (P-eq) and at high temperature. Calcination under these conditions becomes extremely slow. The in situ XRD analysis presented here suggests the presence of an intermediate metastable CaO* phase stemming from the parent CaCO3 structure. According to the reaction mechanism proposed elsewhere, the exothermicity of the CaO* -> CaO transformation and high values of P/P-eq inhibit the nucleation of CaO at high temperatures. The wt% of CaO* remains at a relatively high level during slow calcination. Two diverse stages have been identified in the evolution of CaO crystallite size, L. Initially, L increases with CaCO3 conversion, following a logarithmic law. Slow calcination allows the crystallite size to grow up from a few nanometers at nucleation up to around 100 nm near the end of conversion. Otherwise, quick calcination at relatively lower CO2 concentrations limits CaO crystallite growth. Once calcination reaches an advanced state, the presence of CaO* drops to zero and the rate of increase of the CaO crystallite size is significantly hindered. Arguably, the first stage in CaO crystallite growth is driven by aggregation of the metastable CaO* nanocrystals, due to surface attractive forces, whereas the second one is consistent with sintering of the aggregated CaO crystals, and persists with time after full calcination is attained. Our analysis shows that the main mechanism responsible for the increase of CaO crystallite size (and thus for undermining the reactivity of the CaO) under high CO2 partial pressure is enhanced aggregation, whereas CaO sintering is relatively less relevant, as would be expected for calcination temperatures well below the Tamman temperature.
引用
收藏
页码:21912 / 21926
页数:15
相关论文
共 42 条
[1]   Demonstration of steady state CO2 capture in a 1.7 MWth calcium looping pilot [J].
Arias, B. ;
Diego, M. E. ;
Abanades, J. C. ;
Lorenzo, M. ;
Diaz, L. ;
Martinez, D. ;
Alvarez, J. ;
Sanchez-Biezma, A. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2013, 18 :237-245
[2]  
Barin I., 1997, Thermochemical data of pure substances
[3]  
BERUTO D, 1976, NATURE, V263, P221, DOI 10.1038/263221a0
[4]   USE OF LANGMUIR METHOD FOR KINETIC STUDIES OF DECOMPOSITION REACTIONS - CALCITE (CACO3) [J].
BERUTO, D ;
SEARCY, AW .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS I, 1974, 70 :2145-2153
[5]   Microstructure, kinetic, structure, thermodynamic analysis for calcite decomposition: free-surface and powder bed experiments [J].
Beruto, DT ;
Searcy, AW ;
Kim, MG .
THERMOCHIMICA ACTA, 2004, 424 (1-2) :99-109
[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]  
Boynton R.S., 1980, Chemistry and Technology of Lime and Limestone
[8]   The Prout-Tompkins rate equation in solid-state kinetics [J].
Brown, ME .
THERMOCHIMICA ACTA, 1997, 300 (1-2) :93-106
[9]  
Bruker A., 2009, TOPAS 4 2 USER MANUA
[10]   Experimental Validation of the Calcium Looping CO2 Capture Process with Two Circulating Fluidized Bed Carbonator Reactors [J].
Charitos, Alexander ;
Rodriguez, Nuria ;
Hawthorne, Craig ;
Alonso, Monica ;
Zieba, Mariusz ;
Arias, Borja ;
Kopanakis, Georgios ;
Scheffknecht, Guenter ;
Carlos Abanades, Juan .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (16) :9685-9695