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Modeling study of oil shale pyrolysis in rotary drum reactor by solid heat carrier

机译:固体传热器在转鼓式反应器中油页岩热解建模研究

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The mathematic model of oil shale thermal decomposition (pyrolysis) was constructed on the base of analysis of available experimental data. The model was applied to the engineering procedure that simulates the Galoter process, namely, pyrolysis of oil shale in a horizontal rotary drum reactor in contact with fine-grained solid heat carrier (hot ash). The model includes the kinetics of organic matter (kerogen) decomposition, the processes of heat and mass transfer inside of single oil shale particle, polydispersity of the particles, their fragmentation, and the secondary chemical reactions such as the carbonization of the emitted shale oil on the ash particles as well as shale oil decomposition the free volume of the reactor. Calculations show that the secondary reactions lead to reduce the shale oil yield from 0.27 to 0.13 kg/kg of dry shale, what is close to operating data of the various industrial units based on the Galoter technology. (C) 2015 Published by Elsevier B.V.
机译:在对现有实验数据进行分析的基础上,建立了油页岩热分解(热解)数学模型。该模型已应用于模拟Galoter过程的工程程序,即在与细粒固体热载体(热灰分)接触的水平旋转鼓式反应器中油页岩的热解。该模型包括有机物(干酪根)分解的动力学,单个油页岩颗粒内部的传热和传质过程,颗粒的多分散性,它们的破碎以及次级化学反应,例如排放的页岩油的碳化。灰分以及页岩油会分解反应器的自由体积。计算表明,次级反应使页岩油的产量从干页岩的0.27千克/千克降低至0.13千克/千克,这与基于加洛特技术的各种工业装置的运行数据相近。 (C)2015由Elsevier B.V.发布

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