SULFATION OF DOLOMITE PARTICLES AT HIGH CO2 PARTIAL PRESSURES

被引:14
作者
FUERTES, AB
VELASCO, G
ALVAREZ, T
FERNANDEZ, MJ
机构
[1] Instituto Nacional del Carbón, 33080 Oviedo
关键词
CARBON DIOXIDE; DOLOMITE; HIGH PARTIAL PRESSURE; SULFATION;
D O I
10.1016/0040-6031(94)02067-X
中图分类号
O414.1 [热力学];
学科分类号
摘要
The sulfation reaction of half-calcined dolomite particles at high CO2 partial pressures (around 1 bar) was investigated. The experiments were carried out in two different reactors: (a) a thermogravimetric analysis system (slow heating rates) and (b) a shock-microreactor (rapid heating rates). The experiments were carried out under isothermal conditions at temperatures between 650 and 875 degrees C. A natural dolomite sample was used. Different particle sizes were tested: 26, 128, 256 and 512 mu m. Under reaction conditions employed in the experiments (P-CO2 approximate to 1 atm and T < 900 degrees C), half-calcination of dolomite particles takes place and the sulfation reaction occurs between CaCO3 . MgO and SO2. The CaCO3 is the only active species during sulfation. The particle size and temperature have a strong influence on the variation in extent of conversion with time. Two different stages can be distinguished in the sulfation of half-calcined dolomite particles; chemical control at the onset of reaction and diffusional control at longer reaction times. When the sulfation reaction is carried out under conditions similar to those existing in a boiler (high heating rates and simultaneous calcination and sulfation), the measured reaction rates are higher than those observed from thermogravimetric experiments. At X = 0.1 an activation energy of 34 kcal mol(-1) (142 kJ mol(-1)) was measured. This value suggests that the process is controlled by a solid state diffusion mechanism.
引用
收藏
页码:63 / 78
页数:16
相关论文
共 23 条
[1]   CALCIUM OXIDE-CARBON DIOXIDE SYSTEM IN PRESSURE RANGE 1-300 ATMOSPHERES [J].
BAKER, EH .
JOURNAL OF THE CHEMICAL SOCIETY, 1962, (FEB) :464-&
[2]   EFFECT OF SPECIFIC SURFACE-AREA ON THE REACTIVITY OF CAO WITH SO2 [J].
BORGWARDT, RH ;
BRUCE, KR .
AICHE JOURNAL, 1986, 32 (02) :239-246
[3]  
BORGWARDT RH, 1972, ENVIRON SCI TECHNOL, V4, P350
[4]   DECOMPOSITION EQUILIBRIA FOR CALCIUM AND MAGNESIUM SULPHATES [J].
DEWING, EW ;
RICHARDSON, FD .
TRANSACTIONS OF THE FARADAY SOCIETY, 1959, 55 (04) :611-615
[5]   EQUILIBRIA IN SYSTEMS SO2-CO2-MMO [J].
ERDOS, E .
COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1962, 27 (09) :2152-&
[6]   STUDY OF THE DIRECT SULFATION OF LIMESTONE PARTICLES AT HIGH CO2 PARTIAL PRESSURES [J].
FUERTES, AB ;
VELASCO, G ;
FUENTE, E ;
ALVAREZ, T .
FUEL PROCESSING TECHNOLOGY, 1994, 38 (03) :181-192
[7]   ANALYSIS OF THE DIRECT SULFATION OF CALCIUM-CARBONATE [J].
FUERTES, AB ;
VELASCO, G ;
FERNANDEZ, MJ ;
ALVAREZ, T .
THERMOCHIMICA ACTA, 1994, 242 :161-172
[8]  
FUERTES AB, 1993, CHEM ENG RES DES, V71, P421
[9]   SULFUR RETENTION BY LIMESTONE PARTICLES UNDER PFBC CONDITIONS [J].
FUERTES, AB ;
VELASCO, G ;
FUENTE, E ;
PARRA, JB ;
ALVAREZ, T .
FUEL PROCESSING TECHNOLOGY, 1993, 36 (1-3) :65-71
[10]  
GARCIALABIANO F, 1992, CAN J CHEM ENG, V70, P734