A note on use of the CO2-ethane azeotrope as new feed of reforming process using mathematical modeling

被引:4
|
作者
Tavan, Yadollah [1 ]
机构
[1] NIGC, Tehran, Iran
关键词
CO2; Ethane; Industrial reforming process; Mathematical modeling; Coke formation; EXTRACTIVE DISTILLATION; STEAM REFORMER; METHANE; OPTIMIZATION; HYDROGEN; ETHANE; GAS; SIMULATION; DESIGN;
D O I
10.1016/j.jngse.2014.08.004
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The azeotropes are always considered as a serious problem in chemical industries and most of the published researches on the subject of CO2-ethane azeotropic process are focused on distillation columns and heat exchangers, in order to separate these components. The present study is aimed to remove this azeotrope with the help of reaction and the azeotropic mixture is introduced to an industrial reformer to produce syngas (H-2 and CO), as a novel work. In order to simulate reforming process, two dimensional mathematical modeling is proposed and coke formation as main problem of reforming process is thermodynamically investigated. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:275 / 282
页数:8
相关论文
共 50 条
  • [1] Extractive distillation for CO2-ethane azeotrope separation
    Lastari, Fonny
    Pareek, Vishnu
    Trebble, Mark
    Tade, Moses O.
    Chinn, Daniel
    Tsai, Nancy C.
    Chan, Kaman I.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2012, 52 : 155 - 161
  • [2] TO BREAK AN AZEOTROPE - THE USE OF NORMAL-PENTANE TO BREAK THE CO2-ETHANE AZEOTROPE, FOR CO2 EOR GAS PROCESSING
    HONG, JH
    KOBAYASHI, R
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (03): : 736 - 741
  • [3] Feed-splitting technique in the extractive distillation of CO2-ethane azeotropic process
    Tavan, Yadollah
    Shahhosseini, Shahrokh
    Hosseini, Seyyed Hossein
    SEPARATION AND PURIFICATION TECHNOLOGY, 2014, 122 : 47 - 53
  • [4] TO BREAK AN AZEOTROPE. THE USE OF n-PENTANE TO BREAK THE CO2-ETHANE AZEOTROPE, FOR CO2 EOR GAS PROCESSING.
    Hong, Jane H.
    Kobayashi, Riki
    Industrial & Engineering Chemistry, Process Design and Development, 1986, 25 (03): : 736 - 741
  • [5] A novel application of reactive absorption to break the CO2-ethane azeotrope with low energy requirement
    Tavan, Yadollah
    Hosseini, Seyyed Hossein
    ENERGY CONVERSION AND MANAGEMENT, 2013, 75 : 407 - 417
  • [6] Alternative extractive distillation system for CO2-ethane azeotrope separation in enhanced oil recovery processes
    Ebrahimzadeh, Edris
    Matagi, Jacob
    Fazlollahi, Farhad
    Baxter, Larry L.
    APPLIED THERMAL ENGINEERING, 2016, 96 : 39 - 47
  • [7] Energy optimization and comparative study of pre- and post-fractionator extractive dividing wall column for the CO2-ethane azeotropic process
    Tavan, Yadollah
    Riazi, Seiied Hadi
    Nozohouri, Mostafa
    ENERGY CONVERSION AND MANAGEMENT, 2014, 79 : 590 - 598
  • [8] A Note on an Integrated Process of Methane Steam Reforming in Junction with Pressure-Swing Adsorption to Produce Pure Hydrogen: Mathematical Modeling
    Tavan, Yadollah
    Hosseini, Seyyed Hossein
    Olazar, Martin
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (51) : 12937 - 12947
  • [9] CO 2 reforming of ethane using Ni-La intermetallic sites within a nanocapsule framework
    Wang, Changzhen
    Liu, Lingji
    Liu, Yupeng
    Yu, Xiaosheng
    Chen, Zhou
    Han, Yaohua
    Wang, Yongzhao
    Zhao, Yongxiang
    CHEMICAL ENGINEERING JOURNAL, 2024, 491
  • [10] Development and Implementation of New Technologies Using Mathematical Modeling of the Rolling Process
    Pankovets, I.A.
    Steel in Translation, 2024, 54 (02) : 87 - 93