Optimization of combustion parameters of carbonized rice husk briquettes in a fixed bed using RSM technique

被引:14
作者
Kipngetich, P. [1 ]
Kiplimo, R. [1 ,2 ]
Tanui, J. K. [3 ]
Chisale, P. C. [4 ]
机构
[1] Pan African Univ, Inst Basic Sci Technol & Innovat, POB 62000-00200, Nairobi, Kenya
[2] Jomo Kenyatta Univ Agr & Technol, Dept Marine Engn & Maritime Operat, POB 62000, Nairobi 00200, Kenya
[3] Dedan Kimathi Univ Technol, Dept Mech Engn, Private Bag 10143, Nyeri, Kenya
[4] Copperbelt Univ, Dept Mech Engn, 4662 Jambo Dr,Riverside Campus,POB 21692, Kitwe, Zambia
关键词
Fixed bed; Briquette combustion; Rice husks briquettes; Box-Behnken design; Response surface methodology; Optimization; DOMESTIC COOKING APPLICATIONS; IGNITION FRONT PROPAGATION; MUNICIPAL SOLID-WASTES; BIOMASS COMBUSTION; FUEL PROPERTIES; PACKED-BEDS; AIR-FLOW; GASIFICATION; PARTICLES; PELLETS;
D O I
10.1016/j.renene.2022.07.130
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study investigates the combustion of carbonized rice husk briquettes in a fixed bed to establish the optimum briquetting and combustion conditions. The combustion properties, namely, the average flame propagation speed, the average burning rates, the reaction zone thickness, maximum flame temperature and the ignition time, were optimized with respect to air-flow rate, binder ratio and particle size using response surface methodology (RSM). Seventeen experiments with different combinations of air-flow rate, binder ratio, and particle sizes, each at three levels set according to Box-Behnken Design (BBD), an RSM technique, were performed. Mathematical models for predicting the responses were developed by fitting experimental data. It was established that the binder and air-mass flux predominantly affected all fuel samples during processing and combustion. Optimal values of the ignition time and reaction zone thickness were established to be 249.08 s and 102.43 mm when air-mass flux, binder ratio and particle size were 0.31 kg/m(2).s, 25% and 2.6 mm, respectively. On the other hand, the optimal peak bed temperature was 1226.25 ? when air-mass flux, binder ratio and particle size were 0.31 kg/m(2).s, 25% and 0.3 mm, respectively.
引用
收藏
页码:61 / 74
页数:14
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