• Title/Summary/Keyword: Vinylbenzyl chloride

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The Preparation and Electrochemical Properties of Pore-filled and Polystyrene-based Anion-exchange Membranes Using Poly(ethylene glycol)methyl Ether Methacrylate (Poly(ethylene glycol)methyl Ether Methacrylate를 이용한 세공충전 폴리스티렌계 음이온 교환막의 제조 및 전기화학적 특성)

  • Mun, Hye Jin;Choi, Jae Hak;Hong, Young Taik;Chang, Bong Jun
    • Membrane Journal
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    • v.25 no.6
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    • pp.515-523
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    • 2015
  • While commercial polystyrene-based ion exchange membranes have simple manufacturing processes, they also possess poor durability due to their brittleness. Poly(ethylene glycol)methyl ether methacrylate with hydrophilic side chains of poly(ethylene glycol) was used as a co-monomer to make the membranes have improved flexibility. Hydrophilicity/hydrophobicity of the anion exchange membranes were able to be adjusted by varying the chain lengths of the poly(ethylene glycol). For the preparation of the anion exchange membranes, a porous PE substrate was immersed into monomer solutions and thermally polymerized. The prepared membranes were subsequently reacted with trimethylamine to produce anion exchange functional groups, Quaternary ammonium salts. The prepared pore-filled anion exchange membranes were evaluated in terms of ion exchange capacity, electric resistance, elongation at break and water uptake.

Development of Pore Filled Anion Exchange Membrane Using UV Polymerization Method for Anion Exchange Membrane Fuel Cell Application (음이온교환막 연료전지 응용을 위한 UV 중합법을 이용한 세공 충진 음이온교환막 개발)

  • Ga Jin Kwak;Do Hyeong Kim;Sang Yong Nam
    • Membrane Journal
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    • v.33 no.2
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    • pp.77-86
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    • 2023
  • In this study, pore-filled ion exchange membranes with low membrane resistance and high hydroxide ion conductivity was developed. To improve alkali durability, a porous substrate made of polytetrafluoroethylene was used, and a copolymer was prepared using monomers 2-(dimethyl amino) ethyl methacrylate (DMAEMA) and vinyl benzyl chloride (VBC) for pores. divinyl benzene (DVB) was used as the cross-linker, and ion exchange membranes were prepared for each cross-linking agent content to study the effect of the cross-linker content on DMAEMA-DVB and VBC-DMAEMA-DVB copolymers. As a result, chemical stability is improved by using a PTFE material substrate, and productivity can be increased by enabling fast photo polymerization at a low temperature by using a low-pressure UV lamp. To confirm the physical and chemical stability of the ion exchange membrane required for an anion exchange membrane fuel cell, tensile strength, and alkali resistance tests were conducted. As a result, as the cross-linking degree increased, the tensile strength increased by approximately 40 MPa, and finally, through the silver conductivity and alkali resistance tests, it was confirmed that the alkaline stability increased as the cross-linking agent increased.

Preparation and Application of Pore-filled PVDF ion Exchange Membranes (Pore-filled PVDF 이온교환막의 제조 및 응용)

  • 변홍식;박병규;홍병표;여광수;윤무홍;강남주
    • Membrane Journal
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    • v.14 no.2
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    • pp.108-116
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    • 2004
  • In this study, the pore-filled ion-exchange membranes were prepared by using the asymmetric PVDF membrane as a nascent membrane. First, the solution of PVBCI having the chlorornethylate aryl ring of 80 percents and DABCO was made with the mixed solvent of THF and DU (8:2). These mixed solution was then, filled in the pores of PVDF membrane, and left for a day to complete the gelation. Finally the pore-filled anion-exchange membrane is obtained fallowed by the amination of the remaining chloromethyl groups with trimethylamine (TMA, 40 wt% in water) forming the positive ammonium ion sites. This 2 step procedure enabled us to produce the pore-filled membranes without change of size, and to control the properties of final membrane with various degree of cross-linking. The results of SEM and AFM showed the polyelectrolyte existed in the pores of nascent membrane as a certain configuration. From the investigation of the solvent affecting much to the permeability and rejection, it was found that the membranes using mixed solvent of THE and DMF (8:2) showed better performances than the membranes produced by THF only. The result of an investigation for the water permeability of the final membrane at low pressure (100 Kpa) showed a typical ultrafiltration membrane's permeability (8 ∼ 10 kg/$m^2$hr) and good values of rejection (55∼60 percent).