• English
    • العربية
  • العربية
  • Login
  • QU
  • QU Library
  •  Home
  • Communities & Collections
  • Help
    • Item Submission
    • Publisher policies
    • User guides
    • FAQs
  • About QSpace
    • Vision & Mission
View Item 
  •   Qatar University Digital Hub
  • Qatar University Institutional Repository
  • Academic
  • Faculty Contributions
  • College of Engineering
  • Chemical Engineering
  • View Item
  • Qatar University Digital Hub
  • Qatar University Institutional Repository
  • Academic
  • Faculty Contributions
  • College of Engineering
  • Chemical Engineering
  • View Item
  •      
  •  
    JavaScript is disabled for your browser. Some features of this site may not work without it.

    Comparative Study of Homogeneous and Heterogeneous Modelling of Water-Gas Shift Reaction with Macro-or Micro-kinetics

    Thumbnail
    View/Open
    Publisher version (You have accessOpen AccessIcon)
    Publisher version (Check access options)
    Check access options
    Date
    2016
    Author
    Saw, Shuey Zi
    Nandong, Jobrun
    Ghosh, Ujjal K.
    Metadata
    Show full item record
    Abstract
    This paper presents critical studies on water-gas shift reaction (WGSR) kinetic models as well as the modelling approaches of the reactor, in which the reaction is conducted - the packed-bed tubular reactor (PBTR). There are two different types of models often used to represent the WGSR kinetics: (1) macro-kinetics and (2) micro-kinetics types. The PBTR models can be divided into homogeneous and heterogeneous types. There have been lots of positive and negative arguments regarding the use of different models for the WGSR reactor simulation and design. So far, no solid evidence regarding which form of kinetics model is considered to be the most accurate and suitable for reactor design and simulation. Answering this question is the main objective of this paper, where several major kinds of kinetic-reactor models are compared based on the same Cu (111) catalyst. The different models are used to predict the CO conversion of the shift reactor and their accuracies are compared against a reported experimental data. The analysis shows that the micro-kinetics gives better accuracy than the macro-kinetics model. Interestingly, the results show that the macro-kinetics model used in the homogeneous reactor modelling can give prediction as accurate as that of the more complex micro-kinetics model provided in the former case, the transfer limitation correction factor is included. The comparison among these different models shall provide a better understanding on the selection of model form when it comes to designing the reactor involved. 2016 The Authors. Published by Elsevier Ltd.
    DOI/handle
    http://dx.doi.org/10.1016/j.proeng.2016.06.467
    http://hdl.handle.net/10576/22681
    Collections
    • Chemical Engineering [‎1196‎ items ]

    entitlement


    Qatar University Digital Hub is a digital collection operated and maintained by the Qatar University Library and supported by the ITS department

    Contact Us | Send Feedback
    Contact Us | Send Feedback | QU

     

     

    Home

    Submit your QU affiliated work

    Browse

    All of Digital Hub
      Communities & Collections Publication Date Author Title Subject Type Language Publisher
    This Collection
      Publication Date Author Title Subject Type Language Publisher

    My Account

    Login

    Statistics

    View Usage Statistics

    About QSpace

    Vision & Mission

    Help

    Item Submission Publisher policiesUser guides FAQs

    Qatar University Digital Hub is a digital collection operated and maintained by the Qatar University Library and supported by the ITS department

    Contact Us | Send Feedback
    Contact Us | Send Feedback | QU

     

     

    Video