Pyrolysis of palm kernel shell using screw-assisted fluidization: effect of heating rate

被引:5
作者
Qureshi, Khan Muhammad [1 ]
Lup, Andrew Ng Kay [2 ,3 ]
Khan, Saima [1 ]
Abnisa, Faisal [4 ]
Daud, Wan Mohd Ashri Wan [1 ]
机构
[1] Univ Malaya, Fac Engn, Dept Chem Engn, Kuala Lumpur 50603, Malaysia
[2] Xiamen Univ Malaysia, Sch Energy & Chem Engn, Jalan Sunsuria, Sepang 43900, Selangor Darul, Malaysia
[3] Xiamen Univ, Coll Chem & Chem Engn, Xiamen 361005, Fujian, Peoples R China
[4] King Abdulaziz Univ, Fac Engn, Dept Chem & Mat Engn, Rabigh 21911, Saudi Arabia
关键词
Pyrolysis; Heating rate; Bio-oil; Helical screw-fluidized bed reactor; Palm Kernel shell; BIO-OIL; OPERATING PARAMETERS; LIQUID FUEL; BIOMASS; YIELD; DEOXYGENATION; REACTOR; CHAR;
D O I
10.1007/s43153-021-00161-y
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pyrolysis product yield and composition are dependent on the characteristics of feedstock and operating parameters. Heating rate is one of the key parameters that has substantial influence on pyrolysis yields and its composition. This study aims to investigate the influence of heating rate on the yield and the composition of pyrolysis products from palm kernel shell feedstock in low, medium and high pyrolysis modes. The pyrolysis experiments were performed at three heating rates ranging from 50 to 275 degrees C/min via screw-assisted fluidization. The process was optimized at the rotation speed of 50 rpm at 500 degrees C. A maximum bio-oil yield of 72.86 wt.% was obtained with 275 degrees C/min heating rate. The liquid yield obtained at 275 degrees C/min heating rate contained higher proportion of organic phase of approximately 42.21 wt.% than the aqueous phase. The presence of oxygenated compounds in the organic phase at this heating rate was lower than that obtained with low and medium heating rates.
引用
收藏
页码:619 / 629
页数:11
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