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Numerical and Experimental Research on Chemical Looping Pyrolysis of Coal Tar in a Fluidized Bed Reactor

机译:流化床反应器中煤焦油化学循环热解的数值与实验研究

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Simulation and experiment were carried out as a validation methodology to study the chemical looping pyrolysis of coal tar to prepare carbon black (CB) in a fluidized bed reactor. The results demonstrate that Fe2O3 is reduced to FeO, Fe3O4, and a limited amount of Fe after the Fe-based oxygen carrier (OC) reacted with the coal tar. The gas products mainly consisted of H-2 and CO, and transmission electron microscopy shows that the particle sizes of CB were in decent agreement with the simulation and the size of a single carbon sphere was approximately 40 nm. There were regular changes of the OC particle sizes during the redox process, and the OC particle size was reducing when the oxygen was releasing and was increasing when the oxygen was gaining. Therefore, the OC particle size variation contributes a suitable method to characterize the evolution of the oxygen carrying capacity. The simulations reveal the mechanisms of the chemical looping pyrolysis of coal tar with the reaction models.
机译:进行模拟和实验作为验证方法,以研究流化床反应器中煤焦油的化学循环热解制备炭黑(CB)。结果表明,在铁基氧气载体(OC)与煤焦油反应后,Fe2O3还原为FeO,Fe3O4和有限量的Fe。气体产物主要由H-2和CO组成,透射电子显微镜显示,CB的粒径与模拟结果吻合良好,单个碳球的粒径约为40 nm。氧化还原过程中OC粒径有规律的变化,释放氧时OC粒径减小,而获得氧时OC粒径增大。因此,OC粒径的变化有助于表征氧承载能力的演变。模拟结果揭示了反应模型对煤焦油化学循环热解的机理。

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