CIRCULATING FLUIDIZED-BED COMBUSTION OF A HIGH-SULFUR EASTERN CANADIAN COAL

被引:12
作者
BRERETON, CMH
LIM, CJ
LEGROS, R
ZHAO, J
LI, H
GRACE, JR
机构
[1] Department of Chemical Engineering, University of British Columbia, Vancouver, British Columbia
[2] Fxole Polytechnique de Montréal, Département de génie chimique, Montréal, Quebec, H3C 3A7, C.P. 6079, Succ. "A
[3] Institute for Chemical Metallurgy, Academia Sinica, Beijing
关键词
FLUIDIZATION; COMBUSTION; CIRCULATING FLUIDIZED BED; COAL; NOX; SULFUR CAPTURE;
D O I
10.1002/cjce.5450690406
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Combustion tests were carried out with Minto coal in combination with three different limestones in the University of British Columbia (UBC) pilot scale (152 mm square x 7.3 m tall) circulating fluidized bed combustion (CFBC) unit. Operating conditions were chosen to be typical of those employed in large-scale CFBC power boilers. Recycling of fine particles captured by the secondary cyclone was found to be of considerable importance in increasing sulphur capture, enhancing combustion efficiency and reducing the amount of calcium sulphide in the solids residues. No(x) emissions increased as the Ca:S ratio increased. Local gas concentrations inside the reactor were strongly influenced by the core-annulus solids distribution patterns which characterize circulating fluidized beds.
引用
收藏
页码:852 / 859
页数:8
相关论文
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