CIESC Journal

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重油催化裂化反应集总动力学模型(Ⅲ)工业装置的模拟计算

江洪波; 欧阳福生; 翁惠新   

  1. 华东理工大学石油加工研究所
  • 出版日期:2001-07-25 发布日期:2001-07-25

LUMPED MODEL FOR HEAVY OIL CATALYTIC CRACKING REACTION(Ⅲ)SIMULATION CALCULATION OF COMMERCIAL UNITS

JIANG Hongbo;OUYANG Fusheng;WENG Huixin   

  • Online:2001-07-25 Published:2001-07-25

摘要: 讨论了重油催化裂化动力学模型在工业装置上的应用 ,包括掺炼焦化蜡油和减压渣油能力的预测计算以及催化裂化与芳烃抽提组合工艺的模拟计算

Abstract: The application of heavy oil catalytic cracking 11 lumping kinetic model to commercial unit is discussed in this article,including the simulation calculation of the upper mixing ratio of vacuum residual oil and coking wax oil as well as the combination technique of catalytic cracking and aromatic extraction.The upper mixing ratio simulation provides a way to make the best use of these low grade materials and points out a direction to increase the throughtout capacity of catalytic cracking units.The simulation of the combination technique provides the judgement basis for running the aromatic extraction unit or not.The results of the simulation calculations show that the heavy oil catalytic cracking kinetic model is credible and has good extrapolation ability,and the software for the kinetic model can be used not only for the cases cited but also for other optimization simualtion calculation of FCC units such as choosing the best operation conditions and comparing the different process schemes.