Dynamic Modeling and Simulation of a Commercial Naphtha Catalytic Reforming Process

被引:0
|
作者
胡永有
iit.edu
徐巍华
侯卫锋
苏宏业
褚健
机构
[1] Zhejiang University
[2] National Laboratory of Industrial Control Technology Institute of Advanced Process Control
[3] His current address is Department of Chemical and Environmental Engineering Illinois Institute of Technology
[4] IL 60616
[5] USA. E-mail: huyongy
[6] Chicago
[7] Hangzhou 310027
[8] China
关键词
catalytic reforming; dynamic modeling; simulation; method of lines; process control;
D O I
暂无
中图分类号
TE624 [炼油工艺过程];
学科分类号
081702 ;
摘要
A first principles-based dynamic model for a continuous catalyst regeneration (CCR) platforming process, the UOP commercial naphtha catalytic reforming process, is developed in this paper. The lumping details of the naphtha feed and reaction scheme of the reaction model are given. The process model is composed of the reforming reaction model with catalyst deactivation, the furnace model and the separator model, which is capable of capturing the major dynamics that occurs in this process system. Dynamic simulations are performed based on Gear numerical algorithm and method of lines (MOL), a numerical technique dealing with partial differential equations (PDEs). The results of simulation are also presented. Dynamic responses caused by disturbances in the process system can be correctly predicted through simulations.
引用
收藏
页码:80 / 86
页数:7
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