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Article Navigation >  Green Energy&Environment  > 2016  >  1(3): 266-275
Zhongde Dai, Muhammad Usman, Magne Hillestad, Liyuan Deng. Modelling of a tubular membrane contactor for pre-combustion CO2 capture using ionic liquids: Influence of the membrane configuration, absorbent properties and operation parameters. Green Energy&Environment, 2016, 1(3): 266-275. doi: 10.1016/j.gee.2016.11.006
Citation: Zhongde Dai, Muhammad Usman, Magne Hillestad, Liyuan Deng. Modelling of a tubular membrane contactor for pre-combustion CO2 capture using ionic liquids: Influence of the membrane configuration, absorbent properties and operation parameters. Green Energy&Environment, 2016, 1(3): 266-275. doi: 10.1016/j.gee.2016.11.006
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Modelling of a tubular membrane contactor for pre-combustion CO2 capture using ionic liquids: Influence of the membrane configuration, absorbent properties and operation parameters

doi: 10.1016/j.gee.2016.11.006

  • Department of Chemical Engineering, Norwegian University of Science and Technology (NTNU), Trondheim, 7491, Norway

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  • Corresponding author: E-mail address: deng@nt.ntnu.no (Liyuan Deng)
  • Received date 02 September 2016, Accepted date 18 November 2016, RevRecd date 17 November 2016, Available online 03 December 2016, Publish date 31 October 2016,
    Abstract
  • A membrane contactor using ionic liquids (ILs) as solvent for pre-combustion capture CO2 at elevated temperature (303–393 K) and pressure (20 bar) has been studied using mathematic model in the present work. A comprehensive two-dimensional (2D) mass-transfer model was developed based on finite element method. The effects of liquid properties, membrane configurations, as well as operation parameters on the CO2 removal efficiency were systematically studied. The simulation results show that CO2 can be effectively removed in this process. In addition, it is found that the liquid phase mass transfer dominated the overall mass transfer. Membranes with high porosity and small thickness could apparently reduce the membrane resistance and thus increase the separation efficiency. On the other hand, the membrane diameter and membrane length have a relatively small influence on separation performance within the operation range.

     

    • • Membrane contactor based on physisorption ionic liquids have been applied for pre-combustion CO2 capture. • Porous tubular glass membrane was used in the membrane contactor. • Two-dimensional (2D) mass-transfer model was developed using COMSOL Multiphysics. • The effects of membrane/absorbent properties and operation parameters on CO2 removal efficiency were systematically investigated.
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    • References(60)
  • [1]
    M.E.Boot-Handford Energy & Environ. Sci., 7 (1),pp. 130-189
    [2]
    J.D.Figueroa Int. J. Greenh. Gas Control, 2 (1),pp. 9-20
    [3]
    C.Descamps, C.Bouallou, M.Kanniche Energy, 33 (6),pp. 874-881
    [4]
    S.Smart Energy Environ. Sci., 3 (3),pp. 268-278
    [5]
    X.M.Jie Ind. Eng. Chem. Res., 53 (8),pp. 3305-3320
    [6]
    A.Mansourizadeh, A.F.Ismail J. Hazard. Mater., 171 (1–3),pp. 38-53
    [7]
    S.Zhao J. Membr. Sci., 511 (2016),pp. 180-206
    [8]
    Z.E.Zhang Glob. Nest J., 16 (2),pp. 354-373
    [9]
    Z.Wang Ind. Eng. Chem. Res., 52 (34),pp. 12170-12182
    [10]
    N.Boucif AIChE J., 58 (9),pp. 2843-2855
    [11]
    J.G.Lu Energy Fuels, 24 (2010),pp. 4617-4626
    [12]
    W.F.Zhang, Z.H.Lin
    [13]
    S.Masoumi Energy Fuels, 27 (9),pp. 5423-5432
    [14]
    M.Mehdipour Energy Fuels, 27 (4),pp. 2185-2193
    [15]
    L.H.Cheng J. Membr. Sci., 324 (1–2),pp. 33-43
    [16]
    C.Makhloufi J. Membr. Sci., 455 (2014),pp. 236-246
    [17]
    X.Jie Ind. Eng. Chem. Res., 52 (26),pp. 8783-8799
    [18]
    P.Luis, A.Garea, A.Irabien J. Membr. Sci., 330 (1),pp. 80-89
    [19]
    J.Albo, P.Luis, A.Irabien Ind. Eng. Chem. Res., 49 (21),pp. 11045-11051
    [20]
    Z.Dai, L.Ansaloni, L.Deng Ind. Eng. Chem. Res., 55 (20),pp. 5983-5992
    [21]
    Z.Dai, L.Deng Int. J. Greenh. Gas Control, 54 (2016),pp. 59-69
    [22]
    J.Albo, A.Irabien J. Chem. Technol. Biotechnol., 87 (10),pp. 1502-1507
    [23]
    J.Albo, P.Luis, A.Irabien Desalination Water Treat., 27 (1–3),pp. 54-59
    [24]
    S.J.Zhang Chem. Soc. Rev., 43 (22),pp. 7838-7869
    [25]
    M.A.Malik, M.A.Hashim, F.Nabi Chem. Eng. J., 171 (1),pp. 242-254
    [26]
    E.Santos, J.Albo, A.Irabien J. Membr. Sci., 452 (2014),pp. 277-283
    [27]
    J.Albo, T.Tsuru Ind. Eng. Chem. Res., 53 (19),pp. 8045-8056
    [28]
    J.Deng RSC Adv., 6 (51),pp. 45184-45192
    [29]
    Z.Dai Sci. China Chem., 59 (5),pp. 538-546
    [30]
    Z.Dai J. Membr. Sci., 523 (2017),pp. 551-560
    [31]
    Z.Dai, L.Ansaloni, L.Deng
    [32]
    J.Wang Green Energy Environ., 1 (1),pp. 43-61
    [33]
    J.Chau J. Membr. Sci., 453 (2014),pp. 61-70
    [34]
    K.A.Hoff, H.F.Svendsen Chem. Eng. Sci., 116 (2014),pp. 331-341
    [35]
    M.Saidi J. Nat. Gas Sci. Eng., 18 (2014),pp. 274-285
    [36]
    S.M.R.Razavi Int. J. Greenh. Gas Control, 15 (2013),pp. 142-149
    [37]
    S.Boributh J. Membr. Sci., 401 (2012),pp. 175-189
    [38]
    S.Boributh J. Membr. Sci., 380 (1–2),pp. 21-33
    [39]
    S.Boributh J. Membr. Sci., 372 (1–2),pp. 75-86
    [40]
    S.Shirazian, S.N.Ashrafizadeh Sep. Sci. Technol., 45 (4),pp. 515-524
    [41]
    M.Rezakazemi Chem. Eng. J., 168 (3),pp. 1217-1226
    [42]
    R.Faiz, M.Al-Marzouqi J. Membr. Sci., 365 (1–2),pp. 232-241
    [43]
    Z.E.Zhang Industrial Eng. Chem. Res., 53 (36),pp. 14075-14083
    [44]
    Y.F.Yan Energy Fuels, 28 (9),pp. 5745-5755
    [45]
    J.Jacquemin J. Solut. Chem., 36 (8),pp. 967-979
    [46]
    K.R.Harris, M.Kanakubo, L.A.Woolf J. Chem. Eng. Data, 53 (5),p. 1230
    [47]
    K.R.Harris, M.Kanakubo, L.A.Woolf J. Chem. Eng. Data, 52 (6),pp. 2425-2430
    [48]
    J.Happel Aiche J., 5 (2),pp. 174-177
    [49]
    Z.G.Lei, C.N.Dai, B.H.Chen Chem. Rev., 114 (2),pp. 1289-1326
    [50]
    R.Sander
    [51]
    A.Gabelman, S.-T.Hwang J. Membr. Sci., 159 (1–2),pp. 61-106
    [52]
    J.M.Zheng, Y.Y.Xu, Z.K.Xu Sep. Sci. Technol., 38 (6),pp. 1247-1267
    [53]
    K.E.Gutowski, E.J.Maginn J. Am. Chem. Soc., 130 (44),pp. 14690-14704
    [54]
    Y.Hou, R.E.Baltus Ind. Eng. Chem. Res., 46 (24),pp. 8166-8175
    [55]
    E.R.Gilliland Ind. Eng. Chem., 26 (6),pp. 681-685
    [56]
    S.Mosadegh-Sedghi J. Membr. Sci., 452 (2014),pp. 332-353
    [57]
    H.Kreulen J. Membr. Sci., 78 (3),pp. 197-216
    [58]
    H.Kreulen J. Membr. Sci., 78 (3),pp. 217-238
    [59]
    Z.Wang Energy Fuels, 27 (11),pp. 6887-6898
    [60]
    C.A.Scholes Int. J. Greenh. Gas Control, 42 (2015),pp. 66-74
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