Kinetic modeling of liquid generation from oil shale in fixed bed retort

被引:33
作者
Al-Ayed, Omar S. [1 ]
Suliman, Mohd R. [2 ]
Rahman, Nafi Abdel [3 ]
机构
[1] Fac Engn Technol, Dept Chem Engn, Amman 11134, Jordan
[2] Al Balqa Appl Univ, Marka 11134, Jordan
[3] Al Balqa Appl Univ, Fac Engn Technol, Dept Civil Engn, Amman 11134, Jordan
关键词
Kinetic modeling; Oil shale; Heating rate; Pyrolysis; Fixed bed; Shale oil; PYROLYSIS KINETICS; GAS EVOLUTION;
D O I
10.1016/j.apenergy.2010.02.006
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
Kinetics of shale oil generation in a fixed bed retort is modeled using a second order rate equation. Samples from Ellajjun oil shale deposits are tested in 350-550 degrees C temperatures range. In each run, 400 g are charged to reactor and heated in a range of 2.2-10 degrees C min(-1). Shale oil liquid is condensed at 0 +/- 2 degrees C and its rate measured as function of time and temperature. Increasing heating rate from 2.2 to 10 degrees C min(-1) decreased activation energy from 115 to 71.2 kJ mol(-1) and frequency factor from 2.85 x 10(7) to 9.0 x 10(3) correspondingly. The generated data are modeled using Coats and Redfern differential and integral models. Good agreement has been obtained. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2273 / 2277
页数:5
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