COMPARISON OF COAL PYROLYSIS PRODUCT DISTRIBUTIONS FROM 3 CAPTIVE SAMPLE TECHNIQUES

被引:66
作者
GONENC, ZS
GIBBINS, JR
KATHEKLAKIS, IE
KANDIYOTI, R
机构
[1] Department of Chemical Engineering and Chemical Technology, Imperial College, University of London, London, SW7 2AZ, Prince Consort Road
关键词
pyrolysis of coal; tar; volatile yield;
D O I
10.1016/0016-2361(90)90104-X
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
Pyrolysis tar and char yields were measured at atmospheric pressure between 400-800 °C in three reactors with significantly different design characteristics: a fluidized bed; a wire-mesh reactor; and a 'hot-rod' fixed bed reactor. Ranges of conditions under which results were generally in good agreement were identified using a common sample of Linby (low rank British bituminous) coal. Differences highlighted important non-ideal characteristics in the behaviour of all three systems. The causes of these non-idealities and their implications for the interpretation of pyrolysis data from the three types of reactors are discussed in detail. © 1990.
引用
收藏
页码:383 / 390
页数:8
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