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
  • [41] Control of Product Distribution of Fischer-Tropsch Synthesis with a Novel Rotating Packed-Bed Reactor: From Diesel to Light Olefin
    Chen, Jian-Feng
    Liu, Yi
    Zhang, Yi
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (25) : 8700 - 8703
  • [42] Utilising a radial flow, spherical packed-bed reactor for auto thermal steam reforming of methane to achieve a high capacity of H2 production
    Iranshahi, Davood
    Salimi, Parisa
    Pourmand, Zahra
    Saeidi, Samrand
    Klemes, Jiri Jaromir
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2017, 120 : 258 - 267
  • [43] Continuous lipase-catalyzed synthesis of hexyl laurate in a packed-bed reactor: optimization of the reaction conditions in a solvent-free system
    Ju, Hen-Yi
    Yang, Cheng-Kang
    Yen, Yue-Horng
    Shieh, Chwen-Jen
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2009, 84 (01) : 29 - 33
  • [44] Optimization Using Response Surface Methodology (RSM) for Biodiesel Synthesis Catalyzed by Radiation-Induced Kenaf Catalyst in Packed-Bed Reactor
    Zabaruddin, Nur Haryani
    Abdullah, Luqman Chuah
    Mohamed, Nor Hasimah
    Choong, Thomas Shean Yaw
    PROCESSES, 2020, 8 (10) : 1 - 18
  • [45] Enzymatic synthesis of lard-based ascorbyl esters in a packed-bed reactor: Optimization by response surface methodology and evaluation of antioxidant properties
    Zhao, Haizhen
    Liu, Jianwei
    Lv, Fengxia
    Ye, Ran
    Bie, Xiaomei
    Zhang, Chong
    Lu, Zhaoxin
    LWT-FOOD SCIENCE AND TECHNOLOGY, 2014, 57 (01) : 393 - 399
  • [46] Enzymatic Synthesis of Ethyl Esters from Waste Oil Using Mixtures of Lipases in a Plug-Flow Packed-Bed Continuous Reactor
    Poppe, Jakeline Kathiele
    Matte, Carla Roberta
    de Freitas, Vitoria Olave
    Fernandez-Lafuente, Roberto
    Rodrigues, Rafael C.
    Zichia Ayub, Marco Antonio
    BIOTECHNOLOGY PROGRESS, 2018, 34 (04) : 952 - 959
  • [47] Greener Synthesis of Pristane by Flow Dehydrative Hydrogenation of Allylic Alcohol Using a Packed-Bed Reactor Charged by Pd/C as a Single Catalyst
    Kasakado, Takayoshi
    Hirobe, Yuki
    Furuta, Akihiro
    Hyodo, Mamoru
    Fukuyama, Takahide
    Ryu, Ilhyong
    MOLECULES, 2021, 26 (19):
  • [48] Dimethyl Ether Synthesis with in situ H2O Removal in Fixed-Bed Membrane Reactor: Model and Simulations
    Iliuta, I.
    Larachi, F.
    Fongarland, P.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (15) : 6870 - 6877
  • [49] Continuous-flow synthesis of di-(2-ethylhexyl) peroxydicarbonate in a packed-bed microreactor: Process optimization and kinetic modeling
    Liu, Yushu
    Shang, Minjing
    Liu, Saier
    Xue, Xiao
    Zhong, Zihao
    Niu, Qiang
    Su, Yuanhai
    CHEMICAL ENGINEERING SCIENCE, 2024, 299
  • [50] A novel dynamic membrane reactor concept with radial-flow pattern for reacting material and axial-flow pattern for sweeping gas in catalytic naphtha reformers
    Iranshahi, Davood
    Pourazadi, Ehsan
    Paymooni, Khadijeh
    Rahimpour, Mohammad Reza
    AICHE JOURNAL, 2012, 58 (04) : 1230 - 1247