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作 者:胡永有 iit.edu 徐巍华 侯卫锋 苏宏业 褚健
机构地区:[1]His current address is Department of Chemical and Environmental Engineering Illinois Institute of Technology, Chicago, IL 60616, USA. E-mail: huyongy [2]National Laboratory of Industrial Control Technology Institute of Advanced Process Control, Zhejiang University, Hangzhou 310027, China
出 处:《Chinese Journal of Chemical Engineering》2005年第1期74-80,共7页中国化学工程学报(英文版)
基 金:SupportedbytheNationalOutstandingYouthScienceFoundationofChina(No.60025308)NationalKeyTechnologiesR&DPrograminthe10thFive-YearPlan(No.2001BA204B01).
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.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.
关 键 词:catalytic reforming dynamic modeling SIMULATION method of lines process control
分 类 号:TE624[石油与天然气工程—油气加工工程]
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