Combustion of coffee husks

被引:104
作者
Saenger, M
Hartge, EU
Werther, J [1 ]
Ogada, T
Siagi, Z
机构
[1] Tech Univ Hamburg Harburg, D-21071 Hamburg, Germany
[2] Moi Univ, Dept Prod Engn, Eldoret, Kenya
关键词
coffee husks; combustion mechanisms; ash problems; N2O and NOx emissions;
D O I
10.1016/S0960-1481(00)00106-3
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Combustion mechanisms of two types of coffee husks have been studied using single particle combustion techniques as well as combustion in a pilot-scale fluidised bed facility (FBC), 150 mm in diameter and 9 m high. Through measurements of weight-loss and particle temperatures, the processes of drying, devolatilisation and combustion of coffee husks were studied. Axial temperature profiles in the FBC were also measured during stationary combustion conditions to analyse the location of volatile release and combustion as a function of fuel feeding mode. Finally the problems of ash sintering were analysed. The results showed that devolatilisation of coffee husks (65-72% volatile matter, raw mass) starts at a low temperature range of 170-200 degreesC and takes place rapidly. During fuel feeding using a non water-cooled system, pyrolysis of the husks took place in the feeder tube leading to blockage and non-uniform fuel flow. Measurements of axial temperature profiles showed that during under-bed feeding, the bed and freeboard temperatures were more or less the same, whereas for over-bed feeding, freeboard temperatures were much higher, indicating significant combustion of the volatiles in the freeboard. A major problem observed during the combustion of coffee husks was ash sintering and bed agglomeration. This is due to the low melting temperature of the ash, which is attributed to the high contents of K2O (36-38%) of the coffee husks. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:103 / 121
页数:19
相关论文
共 29 条
[1]  
Adams M.R., 1987, COFFEE TECHNOLOGY, P257
[2]  
AGARWAL PK, 1989, ENG RES DES, P457
[3]  
Bapat D W, 1997, PROC 14 INT C FBC, P165
[4]  
CHEN G, 1997, P 14 INT C FLUID BED, P175
[5]  
CROISET G, 1994, P 8 EUR BIOM C LOND, P2095
[6]  
*ENV RES MAN, 1996, PREL ENV ASS COFF PR
[7]  
Grubor B. G., 1995, P 13 INT C FLUID BED, V1, P515
[8]  
Hellwig G., 1985, ENERGY BIOMASS, P793
[9]  
Johnsson JE, 1991, P 11 INT C FLUID BED, P1389
[10]  
KLEIN MR, 1994, VGB KRAFTWERKTECHNIK, V74, P1071