A novel axial-flow spherical packed-bed membrane reactor for dimethyl ether synthesis: Simulation and optimization

被引:24
|
作者
Samimi, F. [1 ]
Bayat, M. [1 ]
Karimipourfard, D. [1 ]
Rahimpour, M. R. [1 ]
Keshayarz, P. [1 ]
机构
[1] Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Iran
关键词
Dimethyl ether synthesis; Spherical reactor; Selective membrane; Differential evolution; METHANOL DEHYDRATION; COMPOSITE CATALYSTS; SYNGAS; DME;
D O I
10.1016/j.jngse.2013.03.001
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
In order to improve the performance of conventional tubular reactors, the concept of spherical membrane reactors has been proposed as an alternative to eliminate the problem of pressure drop and to increase the production rate. Regarding this, a novel axial-flow spherical packed-bed membrane reactor (AF-SPMR) has been developed for dehydration of methanol. This configuration consists of two concentric spheres in which dimethyl ether (DME) synthesis occurs in the inner sphere coated by a water perm-selective membrane. The operating conditions as well as length per radius for the AF-SPMR were optimized using differential evolution (DE) method to maximize the mole fraction of DME in the outlet point of the reactor. A comparison was made between the optimized AF-SPMR (OAF-SPMR), AF-SPMR, axial-flow spherical packed-bed reactor (AF-SPR) and the conventional reactor (CR). The optimization results indicate the superiority of OAF-SPMR to all previous configurations due to achieving 13.5% increase in the mole fraction of DME. In addition to much lower pressure drop in AF-SPR (nearly 98% reduction); considerably higher production of DME in AF-SPMR represents the main advantages of this configuration in comparison with CR. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:42 / 51
页数:10
相关论文
共 50 条
  • [21] Development of a flat membrane microchannel packed-bed reactor for scalable aerobic oxidation of benzyl alcohol in flow
    Wu, Gaowei
    Cao, Enhong
    Ellis, Peter
    Constantinou, Achilleas
    Kuhn, Simon
    Gavriilidis, Asterios
    CHEMICAL ENGINEERING JOURNAL, 2019, 377
  • [22] Mathematical Modeling and Optimization of Syngas Production Process: A Novel Axial Flow Spherical Packed Bed Tri-Reformer
    Karimipourfard, Dornaz
    Nemati, Nasrin
    Bayat, Mehdi
    Samimi, Fereshteh
    Rahimpour, Mohammad Reza
    CHEMICAL PRODUCT AND PROCESS MODELING, 2018, 13 (02):
  • [23] Simulation of Direct Dimethyl Ether Synthesis in a Slurry Reactor by Recirculation and Axial Dispersion Models
    Ghorbaei, S. Zare
    Ebrahim, H. Ale
    ENERGY TECHNOLOGY, 2015, 3 (06) : 587 - 600
  • [24] Synthesis of Geraniol Esters in a Continuous-Flow Packed-Bed Reactor of Immobilized Lipase: Optimization of Process Parameters and Kinetic Modeling
    Harshada M. Salvi
    Manoj P. Kamble
    Ganapati D. Yadav
    Applied Biochemistry and Biotechnology, 2018, 184 : 630 - 643
  • [25] Synthesis of Geraniol Esters in a Continuous-Flow Packed-Bed Reactor of Immobilized Lipase: Optimization of Process Parameters and Kinetic Modeling
    Salvi, Harshada M.
    Kamble, Manoj P.
    Yadav, Ganapati D.
    APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2018, 184 (02) : 630 - 643
  • [26] Modeling, simulation and control of dimethyl ether synthesis in an industrial fixed-bed reactor
    Farsi, M.
    Eslamloueyan, R.
    Jahanmiri, A.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2011, 50 (01) : 85 - 94
  • [27] Validation of a novel open-source work-flow for the simulation of packed-bed reactors
    Boccardo, Gianluca
    Augier, Frederic
    Haroun, Yacine
    Ferre, Daniel
    Marchisio, Daniele L.
    CHEMICAL ENGINEERING JOURNAL, 2015, 279 : 809 - 820
  • [28] Validation of a novel open-source work-flow for the simulation of packed-bed reactors
    Boccardo, Gianluca
    Augier, Frédéric
    Haroun, Yacine
    Ferré, Daniel
    Marchisio, Daniele L.
    Chemical Engineering Journal, 2015, 279 : 809 - 820
  • [29] Enhancement in Research Octane Number and Hydrogen Production via Dynamic Optimization of a Novel Spherical Axial-Flow Membrane Naphtha Reformer
    Rahimpour, Mohammad Reza
    Iranshahi, Davood
    Paymooni, Khadijeh
    Pourazadi, Ehsan
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (01) : 398 - 409
  • [30] Characteristics of integrated micro packed bed reactor-heat exchanger configurations in the direct synthesis of dimethyl ether
    Hayer, Fatemeh
    Bakhtiary-Davijany, Hamidreza
    Myrstad, Rune
    Holmen, Anders
    Pfeifer, Peter
    Venvik, Hilde J.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 70 : 77 - 85