Minimum fluidization velocities of binary and ternary biomass mixtures with silica sand

被引:8
|
作者
Soanuch, Chaiwat [1 ]
Korkerd, Krittin [1 ]
Piumsomboon, Pornpote [1 ,2 ]
Chalermsinsuwan, Benjapon [1 ,2 ]
机构
[1] Chulalongkorn Univ, Fac Sci, Fuels Res Ctr, Dept Chem Technol, 254 Phayathai Rd, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Ctr Excellence Petrochem & Mat Technol, 254 Phayathai Rd, Bangkok 10330, Thailand
关键词
Fluidized bed; Fluidization; Minimum fluidization velocity; Binary biomass mixture; Ternary biomass mixture; Silica sand; FLOW CHARACTERIZATION; COMBUSTION; PARTICLES; SIZE; SHAPE; BEDS;
D O I
10.1016/j.egyr.2020.08.026
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
Minimum fluidization velocity is an important property which can influence the hydrodynamics and chemical conversion in fluidized bed reactor. Most of the fluidized bed boilers usually mix raw biomass solid particles with medium silica sand solid particles. This is because the biomass supply is varied with the season and location. The objective of this study is to investigate the effect of binary and ternary biomass mixtures with medium solid particles on the obtained minimum fluidization velocity. The experiment was conducted with three types of biomass including, wood chip, rice husk and palm shell waste, together with silica sand. The biomass mixtures were mixed according to the mixture experimental design. The results showed that the mixture of biomass could improve the hydrodynamics inside the system. The minimum fluidization velocity was thus decreased when conducting the experiment with the binary and ternary biomass-silica sand mixtures. The obtained minimum fluidization velocity range was 0.19 to 0.37 m/s. (C) 2020 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:67 / 72
页数:6
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