Bed Agglomeration during the Drying of Mallee Leaf in Fluidized Bed

被引:3
|
作者
Burton, Alan [1 ]
Wu, Hongwei [1 ]
机构
[1] Curtin Univ, Dept Chem Engn, GPO Box U1987, Perth, WA 6845, Australia
基金
澳大利亚研究理事会;
关键词
LIFE-CYCLE ENERGY; WESTERN-AUSTRALIA; CARBON FOOTPRINTS; FAST PYROLYSIS; BIOMASS; DRYER; GASIFICATION; PARTICLES; TECHNOLOGIES; OPTIMIZATION;
D O I
10.1021/acs.iecr.5b04479
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Drying of mallee leaf was carried out in a laboratory fluidized-bed reactor in air at 120-250 degrees C for 15 min. Surprisingly, bed agglomeration takes place even during drying. The bed agglomeration yield (Y-AP), which is the mass of bed agglomerates expressed as the percentage of the total mass of all samples collected from the bed, increases from 5.2% at 120 degrees C to 17.3% at 250 degrees C. Similar to those that took place during biomass pyrolysis, the interaction between biomass and sand bed particles during biomass drying can also be quantified using sand loading (S-L), which is the mass of sand sticking to the biomass particles in the bed (to form bed agglomerates) normalized to the total mass of biomass fed. S-L during biomass drying also follows a similar generic equation (S-L = KR-0.5) as previously reported for biomass pyrolysis for 15 min, where K is analogous to the Arrhenius equation and R is the biomass feed to sand ratio (i.e., the ratio between the total accumulated mass of biomass fed and the total mass of sand in the fluidized bed). The activation energies for bed agglomeration during biomass drying under air and argon atmosphere are estimated to be 19.7 and 29.3 kJ/mol, respectively.
引用
收藏
页码:1796 / 1800
页数:5
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