Simulation, sensitivity analysis and optimization of a commercial continuous catalytic naphtha reformer

被引:5
|
作者
Weifeng, Hou [1 ]
Xiuqiang, Zheng [1 ]
Yanping, Hong [1 ]
Fengyue, Jiang [1 ]
机构
[1] Zhejiang Supcon Software Co., Ltd., 310053, Hangzhou, China
关键词
Calculated values - Industrial units - Kinetic modeling - Kinetics modeling - Operating condition - Operating data - Optimization project - Process Variables;
D O I
10.3923/itj.2013.4953.4958
中图分类号
学科分类号
摘要
In this study, a 20-lumped kinetics model for naphtha catalytic reforming reactions is used to simulate an industrial Continuous Catalytic Reforming (CCR) process. Fair agreement between the calculated and operating data is obtained. The key process variables affecting the aromatics yield are analyzed in detail to guide the selections of operating conditions. Based on the kinetics model and the process variable analyses, process optimization is also studied and the optimization project is then tested in the actual industrial unit about one month. The testing results validate that the aromatics yield increases about 0.49 percent in weight averagely, which is close to the calculated value by process optimization. The optimization project obtained by mathematic computation is proved to be believable and can bring great profits of more than 5,000,000 yuan annually. © 2013 Asian Network for Scientific Information.
引用
收藏
页码:4953 / 4958
相关论文
共 50 条
  • [41] Monitoring and path optimization of catalytic reformer in a refinery: Principal component analysis and A* algorithm application
    Li, Zhi
    Ying, Yuhui
    Yang, Minglei
    Zhao, Liang
    Zhao, Ling
    Du, Wenli
    EXPERT SYSTEMS WITH APPLICATIONS, 2022, 209
  • [42] Simulation and optimization of a naphtha thermal cracking pilot plant
    Shahrokhi, M
    Masoumi, ME
    Sadrameli, M
    Towfighi, J
    IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION, 2003, 22 (01): : 27 - 35
  • [43] Modeling and simulation of four catalytic reactors in series for naphtha reforming
    Ancheyta, J
    Villafuerte-Macías, E
    Díaz-García, L
    González-Arredondo, E
    ENERGY & FUELS, 2001, 15 (04) : 887 - 893
  • [44] Modeling and Simulation of Moving Bed Reactor for Catalytic Naphtha Reforming
    Hongjun, Z.
    Mingliang, S.
    Huixin, W.
    Zeji, L.
    Hongbo, J.
    PETROLEUM SCIENCE AND TECHNOLOGY, 2010, 28 (07) : 667 - 676
  • [45] Molecular-Level Modeling of Naphtha Continuous Catalytic Reforming Process
    Wu, Jian
    Chen, Guoxing
    Chen, Aiqing
    Gao, Zhao
    Wu, Xi
    Cheng, Haiyang
    Li, Yifei
    Wang, Yongchun
    Qian, Zhiming
    Zhang, Xiaosong
    Xu, Chunming
    Chen, Zhengyu
    Zhang, Linzhou
    CHEMICAL ENGINEERING SCIENCE, 2025, 309
  • [46] On-line production quality prediction for a commercial naphtha catalytic reforming process
    Hou, Weifeng
    Zhao, Lujun
    Zhang, Liming
    Wang, Guihong
    Information Technology Journal, 2013, 12 (18) : 4553 - 4560
  • [47] ANALYSIS IMPROVES CATALYTIC REFORMER TROUBLESHOOTING.
    Pistorius, J.T.
    Oil and Gas Journal, 1985, 83 (23): : 146 - 151
  • [48] Failure analysis of catalytic steam reformer tubes
    Tawancy, HM
    Ul-Hamid, A
    Mohammed, AI
    Abbas, NM
    ANTI-CORROSION METHODS AND MATERIALS, 2005, 52 (06) : 337 - 344
  • [49] Modelling and simulation of a catalytic autothermal methane reformer with Rh catalyst
    Scognamiglio, Diego
    Russo, Lucia
    Maffettone, Pier Luca
    Salemme, Lucia
    Simeone, Marino
    Crescitelli, Silvestro
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (01) : 263 - 275
  • [50] Applying new kinetic and deactivation models in simulation of a novel thermally coupled reactor in continuous catalytic regenerative naphtha process
    Iranshahi, Davood
    Rafiei, Razieh
    Jafari, Mitra
    Amiri, Shahram
    Karimi, Mohsen
    Rahimpour, Mohammad Reza
    CHEMICAL ENGINEERING JOURNAL, 2013, 229 : 153 - 176