Preparation and properties of PVDF hollow fiber membrane for desalination using air gap membrane distillation

被引:29
作者
Lin, Long [1 ,2 ]
Geng, Hongxin [1 ,2 ,3 ]
An, Yaxin [1 ,2 ]
Li, Pingli [1 ,2 ]
Chang, Heying [1 ,2 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
[2] Tianjin Univ, Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin 300072, Peoples R China
[3] All China Federat Supply & Mkt Cooperat, Tianjin Recyclable Resources Inst, Tianjin 300191, Peoples R China
关键词
Membrane preparation; Polyvinylidene fluoride; Thermally induced phase separation; Membrane distillation; BICONTINUOUS STRUCTURE-MEMBRANE; INDUCED PHASE-SEPARATION; POLYVINYLIDENE FLUORIDE; DILUENT; INVERSION; CASCADE; MODULES; DESIGN; SYSTEM;
D O I
10.1016/j.desal.2015.04.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The polyvinylidene fluoride (PVDF) hollow fiber membrane was prepared for membrane distillation through thermally induced phase separation (TIPS) using glyceryl triacetate (GTA) and dibutyl sebacate (DBS) as the mixed diluents. The bicontinuous structure of membrane pore was obtained in the case: PVDF/GTA/DBS is 25 wt.%:22.5 wt.%:62.5 wt.%, and the coagulation bath is the water of 20 degrees C. The membrane porosity and mechanical strength are 0.64 and 2.7 MPa, respectively. The PVDF membrane was characterized using the measurement of the liquid entry pressure (LEPw), scanning electron microscopy (SEM), mean pore, porosity and mechanical strength. The prepared PVDF membrane was tested in an AGMD process for desalination with 7.0 wt.% NaCl solution as the feed. The permeate water flux (J(D)) and gained output ratio (GOR) simultaneously reach to 5.5 kg/m(2)h and 6.2. The prepared PVDF membrane can be operated continuously for 240 h without any significant change to J(D) and GOR, indicating that the prepared PVDF hollow fiber membrane by TIPS method may be of great potential to be utilized in AGMD process for desalination. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:145 / 153
页数:9
相关论文
共 32 条
  • [1] Ultrafiltration PVDF hollow fibre membranes with interconnected bicontinuous structures produced via a single-step phase inversion technique
    Abed, M. R. Moghareh
    Kumbharkar, S. C.
    Groth, Andrew M.
    Li, K.
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2012, 407 : 145 - 154
  • [2] Potential of membrane distillation in seawater desalination: Thermal efficiency, sensitivity study and cost estimation
    Al-Obaidani, Sulaiman
    Curcio, Efrem
    Macedonio, Francesca
    Di Profio, Gianluca
    Ai-Hinai, Hilal
    Drioli, Enrico
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2008, 323 (01) : 85 - 98
  • [3] An Y., 2013, PREPARATION PVDF FLA
  • [4] Desalination by membrane distillation: A parametric study
    Banat, FA
    Simandl, J
    [J]. SEPARATION SCIENCE AND TECHNOLOGY, 1998, 33 (02) : 201 - 226
  • [5] Brandrup J., 1999, Polymer Handbook, VII
  • [6] Poly(vinylidene fluoride) membranes by phase inversion: the role the casting and coagulation conditions play in their morphology, crystalline structure and properties
    Buonomenna, M. G.
    Macchi, P.
    Davoli, M.
    Drioli, E.
    [J]. EUROPEAN POLYMER JOURNAL, 2007, 43 (04) : 1557 - 1572
  • [7] Numerical Simulation and Optimal Design of AGMD-Based Hollow Fiber Modules for Desalination
    Cheng, Li-Hua
    Wu, Ping-Chung
    Chen, Junghui
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (10) : 4948 - 4959
  • [8] Preparation of porous PVdF membrane via thermally induced phase separation using sulfolane
    Cui, Zhen-Yu
    Du, Chun-Hui
    Xu, You-Yi
    Ji, Gen-Liang
    Zhu, Bao-Ku
    [J]. JOURNAL OF APPLIED POLYMER SCIENCE, 2008, 108 (01) : 272 - 280
  • [9] Integrated membrane - based desalination system
    El-Zanati, E.
    El-Khatib, K. M.
    [J]. DESALINATION, 2007, 205 (1-3) : 15 - 25
  • [10] Experimental study of hollow fiber AGMD modules with energy recovery for high saline water desalination
    Geng, Hongxin
    He, Qingfeng
    Wu, Haoyun
    Li, Pingli
    Zhang, Chunyao
    Chang, Heying
    [J]. DESALINATION, 2014, 344 : 55 - 63