Effects of Ca-based additives on desulfurization during coal pyrolysis

被引:83
作者
Guan, RG [1 ]
Li, W [1 ]
Li, BQ [1 ]
机构
[1] Chinese Acad Sci, Inst Coal Chem, State Key Lab Coal Convers, Taiyuan 030001, Peoples R China
关键词
Ca-based additives; coal; desulfurization; pyrolysis; combustion;
D O I
10.1016/S0016-2361(03)00188-1
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 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
The effects of different Ca-based additives on the sulfur removal of coals during pyrolysis up to 900 degreesC have been studied in a fixed-bed reactor. It was found that Ca(OH)(2) and CaO were quite effective to capture the sulfur-containing gases, 95% of the sulfur evolved from untreated coal was retained in the char by the use of additives. Both the tar yield and the sulfur content of the tar decreased with addition of Ca-based additives. The effect of Ca(OH)(2) was better than that of CaO due to its higher activity, but CaCO3 had little effect because of its higher decomposition temperature (-900 degreesC) than the peak temperature range (400-500 degreesC) of sulfur-containing gases emission. There is remarkable sulfur retention effect with Ca(OH)(2) prepared by impregnation and ultrasonic treatment due to the higher dispersion in coal particles than by simple mechanical mixing. The ultrasonic treatment is the best method with regard to the lowest SO2 release during the char combustion. XRD results showed that the sulfur captured by Ca-based additives during pyrolysis turned into CaS. FeS detected in pyrolysis char without additives disappeared in chars with additives, which indicated that CaO could react with FeS through solid-solid reaction. When the chars with calcium-additives were burned in fixed bed reactor, they gave out less SO2 than the raw coal added with same additives. The best total desulfurization efficiency could reach to about 85%. (C) 2003 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1961 / 1966
页数:6
相关论文
共 14 条
[1]
SULFATION OF PARTIALLY SULFIDED CALCIUM-BASED SORBENTS [J].
ABBASIAN, J ;
REHMAT, A ;
BANERJEE, DD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (08) :1990-1994
[2]
BENJAMIN G, 1999, FUEL, V78, P573
[3]
SELF-DIFFUSION OF IRON AND SULFUR IN FERROUS SULFIDE [J].
CONDIT, RH ;
HOBBINS, RR ;
BIRCHENALL, CE .
OXIDATION OF METALS, 1974, 8 (06) :409-455
[4]
Sulfur distribution within coal pyrolysis products [J].
Czaplicki, A ;
Smolka, W .
FUEL PROCESSING TECHNOLOGY, 1998, 55 (01) :1-11
[5]
THE SULFIDATION OF CALCINED LIMESTONE WITH HYDROGEN-SULFIDE AND CARBONYL SULFIDE [J].
HEESINK, ABM ;
VANSWAAIJ, WPM .
CHEMICAL ENGINEERING SCIENCE, 1995, 50 (18) :2983-2996
[6]
JUAN A, 1997, FUEL, V76, P257
[7]
KUANRONG Q, 1999, FUEL, V78, P225
[8]
Study on the ultrasonic irradiation of coal water slurry [J].
Li, YX ;
Li, BQ .
FUEL, 2000, 79 (3-4) :235-241
[9]
SO2 CAPTURE IN FLUIDIZED-BED BOILERS - RE-EMISSION OF SO2 DUE TO REDUCTION OF CASO4 [J].
LYNGFELT, A ;
LECKNER, B .
CHEMICAL ENGINEERING SCIENCE, 1989, 44 (02) :207-213
[10]
RATE AND DIFFUSIONAL STUDY OF THE REACTION OF CALCIUM-OXIDE WITH SULFUR-DIOXIDE [J].
MARSH, DW ;
ULRICHSON, DL .
CHEMICAL ENGINEERING SCIENCE, 1985, 40 (03) :423-433