Wetting prevention in membrane distillation through superhydrophobicity and recharging an air layer on the membrane surface

被引:114
|
作者
Rezaei, Mohammad [1 ]
Warsinger, David M. [2 ]
Lienhard, John H., V [2 ]
Samhaber, Wolfgang M. [1 ]
机构
[1] Johannes Kepler Univ Linz, Inst Proc Engn, Altenberger Str 69, A-4040 Linz, Austria
[2] MIT, Dept Mech Engn, Rohsenow Kendall Heat Transfer Lab, 77 Massachusetts Ave, Cambridge, MA 02139 USA
关键词
Membrane distillation; Wetting phenomenon; Air recharging; Superhydrophobic membrane; VACUUM MEMBRANE; OPERATIONAL PARAMETERS; NANOFIBROUS MEMBRANES; WATER DESALINATION; FIBER MEMBRANES; PVDF MEMBRANES; MD MEMBRANES; PERFORMANCE; ENHANCEMENT; MODULES;
D O I
10.1016/j.memsci.2017.02.013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Although membrane distillation offers distinctive benefits in some certain areas, i.e., RO concentrate treatment, concentrating solutions in the food industry and solar heat utilization, the occurrence of wetting of the hydrophobic membrane hinders its potential industrial applications. Therefore, wetting prevention is a vital criterion particularly for the treatment of solutions with lower surface tension than water. The present work examines the effect of recharging air bubbles on the membrane surface for the wetting incidence when a surfactant (sodium dodecyl sulfate, SDS) exists in a highly concentrated NaCl aqueous solution. This study shows that the presence of the air bubbles on the surface of the superhydrophobic membrane in a direct contact membrane distillation setup inhibited the occurrence of wetting (similar to 100% salt rejection) even for high concentrations of the surface-active species (up to 0.8 mM SDS) in the feed solution while no undesirable influence on the permeate flux was observed. Introducing air into the feed side of the membrane displaces the liquid which partly tends to penetrate the macro porous structure with air bubbles and therefore increases the liquid entry pressure, and in addition, the simultaneous use of a superhydrophobic membrane enhances the solution contact angle.
引用
收藏
页码:42 / 52
页数:11
相关论文
共 50 条
  • [21] Membrane scaling and prevention techniques during seawater desalination by air gap membrane distillation
    Duong, Hung C.
    Duke, Mikel
    Gray, Stephen
    Cooper, Paul
    Nghiem, Long D.
    DESALINATION, 2016, 397 : 92 - 100
  • [22] STEADY-STATES IN MEMBRANE DISTILLATION - INFLUENCE OF MEMBRANE WETTING
    PENA, L
    DEZARATE, JMO
    MENGUAL, JI
    JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS, 1993, 89 (24): : 4333 - 4338
  • [23] Electrospun dual-layer nonwoven membrane for desalination by air gap membrane distillation
    Woo, Yun Chul
    Tijing, Leonard D.
    Park, Myoung Jun
    Yao, Minwei
    Choi, June-Seok
    Lee, Sangho
    Kim, Seung-Hyun
    An, Kyoung-Jin
    Shon, Ho Kyong
    DESALINATION, 2017, 403 : 187 - 198
  • [24] Design of a superhydrophobic network layer for enhancing the stability and wetting resistance of membrane distillation
    Zhou, Junhao
    Li, Yixin
    Wu, Qiang
    Liu, Ziqiang
    Zhang, Mengmeng
    Hu, Haonan
    Wang, Xuan
    Lu, Xiaolong
    Wu, Chunrui
    SEPARATION AND PURIFICATION TECHNOLOGY, 2025, 364
  • [25] The effects of membrane surface wettability on pore wetting and scaling reversibility associated with mineral scaling in membrane distillation
    Yin, Yiming
    Jeong, Nohyeong
    Tong, Tiezheng
    JOURNAL OF MEMBRANE SCIENCE, 2020, 614
  • [26] Surface engineering for anti-wetting and antibacterial membrane for enhanced and fouling resistant membrane distillation performance
    Ray, Saikat Sinha
    Dangayach, Raghav
    Kwon, Young-Nam
    CHEMICAL ENGINEERING JOURNAL, 2021, 405
  • [27] Nanofiber based triple layer hydro-philic/-phobic membrane - a solution for pore wetting in membrane distillation
    Prince, J. A.
    Rana, D.
    Matsuura, T.
    Ayyanar, N.
    Shanmugasundaram, T. S.
    Singh, G.
    SCIENTIFIC REPORTS, 2014, 4
  • [28] Nanofiber based triple layer hydro-philic/-phobic membrane - a solution for pore wetting in membrane distillation
    J. A. Prince
    D. Rana
    T. Matsuura
    N. Ayyanar
    T. S. Shanmugasundaram
    G. Singh
    Scientific Reports, 4
  • [29] Research progress of membrane fouling and wetting in membrane distillation process for desalination
    Xie S.
    Wen J.
    Pang Z.
    Hou C.
    Li Z.
    Jin D.
    Peng Y.
    Huagong Jinzhan/Chemical Industry and Engineering Progress, 2021, 40 (07): : 3942 - 3956
  • [30] Modeling of pore wetting in vacuum membrane distillation
    Chamani, Hooman
    Matsuura, Takeshi
    Rana, Dipak
    Lan, Christopher Q.
    JOURNAL OF MEMBRANE SCIENCE, 2019, 572 : 332 - 342