A Mechanistic Model on Catalyst Deactivation by Coke Formation in a CSTR Reactor

被引:4
|
作者
Muhammad, Ishaka [1 ,2 ]
Makwashi, Nura [3 ]
Ahmed, Tariq Galadanchi [4 ]
Manos, George [1 ]
Zhao, Donglin [5 ]
机构
[1] UCL, Dept Chem Engn, London WC1E 7JE, England
[2] Zamfara State Coll Educ, Dept Chem, PMB 860272, Maru, Nigeria
[3] Bayero Univ, Dept Chem & Petr Engn, PMB 3011, Kano, Nigeria
[4] Teesside Univ, Sch Comp Engn & Digital Technol, Middlesbrough TS1 3BX, England
[5] London South Bank Univ, Sch Engn, London SE1 0AA, England
关键词
mechanistic modelling; catalyst deactivation; coke formation; CSTR; catalytic cracking; C-8; ALIPHATIC-HYDROCARBONS; LOW-DENSITY POLYETHYLENE; FIXED-BED REACTORS; SKELETAL ISOMERIZATION; 1-PENTENE ISOMERIZATION; CRACKING; CONVERSION; SIMULATION; PYROLYSIS; KINETICS;
D O I
10.3390/pr11030944
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A mechanistic model on catalyst deactivation by coke formation in a continuous stirred tank reactor (CSTR) has been developed in the paper. Catalyst deactivation by coke formation was treated as a surface reaction. Four reaction mechanisms representing coke formation through different routes were proposed. The evolved system of ordinary differential equations (ODEs) was solved numerically using MATLAB. This approach was validated by applying it to the skeletal isomerization of 1-pentene over ferrierite. Simulation results were compared qualitatively to those obtained from the literature. Simulation results indicated that coke formation is an extremely rapid process with fast formation of coke components on the strongest acid sites leading to final coke. The coke deposition is slower at higher residence times resulting in more stable product formation and weaker deactivation. The results obtained from this work revealed that the developed model is indeed able to successfully demonstrate the most essential features of catalyst deactivation by coke formation and are in agreement with the findings in the literature. Future work is aimed to extend the study to different reactors such as a plug flow reactor, in addition to analysis of the reaction system's sensitivity to variables such as temperature and pressure.
引用
收藏
页数:19
相关论文
共 50 条
  • [1] Reactor Model for Heavy Oil Hydrotreating with Catalyst Deactivation Based on Vanadium and Coke Deposition
    Jurado, Javier
    Ancheyta, Jorge
    ENERGY & FUELS, 2022, : 11132 - 11141
  • [2] Coke formation in copper catalyst during cyclohexanol dehydrogenation: Kinetic deactivation model and catalyst characterization
    Simon, Ernesto
    Maria Rosas, Juana
    Santos, Aurora
    Romero, Arturo
    CHEMICAL ENGINEERING JOURNAL, 2013, 214 : 119 - 128
  • [3] Kinetic modeling of hydrocarbon processing and the effect of catalyst deactivation by coke formation
    Froment, G. F.
    CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2008, 50 (01): : 1 - 18
  • [4] Role of pore structure in the deactivation of zeolites (HZSM-5, Hβ and HY) by coke in the pyrolysis of polyethylene in a conical spouted bed reactor
    Elordi, G.
    Olazar, M.
    Lopez, G.
    Castano, P.
    Bilbao, J.
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2011, 102 (1-2) : 224 - 231
  • [5] Modeling of Coke Formation and Catalyst Deactivation in Propane Dehydrogenation Over a Commercial Pt-Sn/γ-Al2O3 Catalyst
    Niknaddaf, S.
    Soltani, M.
    Farjoo, A.
    Khorasheh, F.
    PETROLEUM SCIENCE AND TECHNOLOGY, 2013, 31 (23) : 2451 - 2462
  • [6] Catalyst deactivation by coking and coke dissolving at supercritical conditions
    Manos, G
    1997 JUBILEE RESEARCH EVENT, VOLS 1 AND 2, 1997, : 1185 - 1188
  • [7] Model of an Industrial Reactor for Formaldehyde Production with Catalyst Deactivation
    Braz, Catarina G.
    Matos, Henrique A.
    Mendes, A.
    Rocha, Jorge F.
    Alvim, Ricardo P.
    27TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PT A, 2017, 40A : 121 - 126
  • [8] Kinetic model for hydrocracking of heavy oil in a CSTR involving short term catalyst deactivation
    Martinez, Jeremias
    Ancheyta, Jorge
    FUEL, 2012, 100 : 193 - 199
  • [9] Experiment and modeling of coke formation and catalyst deactivation in n-heptane catalytic cracking over HZSM-5 zeolites
    Ma, Zhenzhou
    Hou, Xu
    Chen, Bochong
    Zhao, Liu
    Yuan, Enxian
    Cui, Tingting
    CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2023, 55 : 165 - 172
  • [10] Model of an industrial multitubular reactor for methanol to formaldehyde oxidation in the presence of catalyst deactivation
    Braz, Catarina G.
    Mendes, Adelio
    Rocha, Jorge
    Alvim, Ricardo
    Matos, Henrique A.
    CHEMICAL ENGINEERING SCIENCE, 2019, 195 : 347 - 355