The catalytic mechanism was proposed and the kinetic mathematical model of the catalytic reaction for obtaining the thermodynamic and kinetic pa.
建立了催化反应的动力学数学模型，获得了催化反应相关的热力学和动力学参数。
Based on three lumping kinetic model of catalytic cracking, the parameters in the model are estimated with actual operation data of a commercial catalytic cracking riser.
本文针对催化裂化工业装置的提升管反应器以三集总催化裂化反应动力学模型为基础，利用工业装置的现场数据对模型中的参数进行了拟合。
It could be of high value to apply the successfully developed kinetic model of naphtha catalytic reforming broadly into process design and plant production optimization.
开发成功的动力学模型能广泛应用于工业装置的工艺设计和优化生产操作，具有重要的实用价值。
The kinetic equation and effective factor of the structured catalytic bag were incorporated into the mathematical model of a catalytic distillation column.
将动力学方程和催化剂捆包的效率因子归入到催化精馏塔的数学模型当中。
A 7-lump kinetic model was proposed for heavy oil catalytic pyrolysis. The reaction network and mathematics expressions were also given.
建立了重油催化裂解七集总动力学模型，给出了模型的反应网络和数学表达式。
The results provide the foundation for establishing the single-event micro-kinetic model of catalytic reforming.
该结果可为催化重整单事件反应动力学模型的建立提供理论基础。
The results provide the foundation for establishing the single-event micro-kinetic model of catalytic reforming.
该结果可为催化重整单事件反应动力学模型的建立提供理论基础。
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