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作 者:Jiang Shubao Jiang Hongbo Li Zhenming Tian Jianhui
机构地区:[1]Research Institute of Petroleum Processing,East China University of Science and Technology,Shanghai 200237 [2]International Joint Research Center of Green Energy Chemical Engineering,East China University of Science and Technology,Shanghai 200237 [3]Petro-Cyber Works Information Technology Co.,Ltd.,Beijing 100007
出 处:《China Petroleum Processing & Petrochemical Technology》2021年第3期90-103,共14页中国炼油与石油化工(英文版)
基 金:This work was supported by the Science and Technology Development Project of SINOPEC,China(No.319026).
摘 要:An approach for the simulation and optimization of continuous catalyst-regenerative process of reforming is proposed in this paper.Compared to traditional method such as finite difference method,the orthogonal collocation method is less time-consuming and more accurate,which can meet the requirement of real-time optimization(RTO).In this paper,the equation-oriented method combined with the orthogonal collocation method and the finite difference method is adopted to build the RTO model for catalytic reforming regenerator.The orthogonal collocation method was adopted to discretize the differential equations and sequential quadratic programming(SQP)algorithm was used to solve the algebraic equations.The rate constants,active energy and reaction order were estimated,with the sum of relative errors between actual value and simulated value serving as optimization objective function.The model can quickly predict the fields of component concentration,temperature and pressure inside the regenerator under different conditions,as well as the real-time optimized conditions for industrial reforming regenerator.
关 键 词:catalytic reforming regenerator KINETICS model orthogonal collocation method real-time optimization
分 类 号:TE624.9[石油与天然气工程—油气加工工程]
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