Oxidation of the sulphurised dolomite produced in the desulphurisation of the gasification gases

被引:10
作者
Alvarez-Rodriguez, Ramon [1 ]
Clemente-Jul, Carmen [1 ]
机构
[1] Tech Univ Madrid UPM, Min Sch, Madrid 28003, Spain
关键词
Calcium sulphide oxidation; Gasification; Dolomite; Coal; CALCIUM-BASED SORBENTS; FIXED-BED REACTOR; COAL-GAS; REGENERABLE SORBENTS; METAL-OXIDES; PERFORMANCE; DECOMPOSITION; SULFIDATION; KINETICS; SO2;
D O I
10.1016/j.fuel.2008.11.035
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
Dolomite reacts with H(2)S to produce calcium sulphide and has been broadly investigated as a desulphurisation agent due to its low-cost and favourable properties. Because CaS reacts with water or water vapour in the environment to regenerate hydrogen sulphide and, therefore, disposal is problematic and the chemical cannot be uses as a landfill material. One of the methods used to make this material inert is oxidation to convert calcium sulphide into calcium sulphate or calcium oxide. In our study, tests were carried out using dolomite from Granada, Spain, that was previously calcined and sulphurised at high temperature with a gas similar to that produced in gasification facilities. To approximate real-scale results, a relatively large amount of substance was used for each sample (100-150 g) and the samples were used in a fixed-bed position. The influence of different conditions, such as grain size, composition of the oxidation gas, gas velocity, bed length and temperature, was them investigated. The final solid products were characterised by X-ray diffraction and chemical analysis and the CO(2), SO(2), H(2)S and COS concentrations in the gases produced during oxidation were analysed by gas chromatography. The results showed that the most influential factor was grain size and that the best oxidant was O(2) mixed with nitrogen. The presence of water vapour increases the residual concentration of CaS in the end product, but increased the CaO content The higher the oxygen concentration and the higher the gas velocity, the lower the residual content of CaS. CO(2) used alone oxidises CaS to produce SO(2) and COS, but at very low rates. It also produces some CS(2) Water vapour used alone can also oxidise the CaS to produce H(2)S and SO(2) but also at very low velocity. At higher oxidation temperature, between 700 degrees C and 850 degrees C, lesser residual CaS is obtained in the oxidised product. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2507 / 2519
页数:13
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