2015
DOI: 10.1007/s12034-015-0878-z
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Cetyltrimethylammonium bromide–silica membrane for seawater desalination through pervaporation

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Cited by 19 publications
(3 citation statements)
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“…Use of oxides of pure Al 2 O 3 , TiO 2 , ZrO 2 , SiO 2 or their combinations for the preparation of ceramic membranes [5,[10][11][12][13][14][15][16][17][18][19][20][21][22][23][24][25][26] with high chemical, mechanical and thermal stabilities are well established [27,28] and are common, but the use of high cost inorganic precursors to obtain these oxides increases the cost as well as requires high sintering temperature (>1100 • C) for fabrication. The use of cheaper precursors such as ball clay, kaolin, quartz, feldspar, CaCO 3 , clay, sand and pyrophyllite for preparation of microfiltration range ceramic membranes have been reported [29,30].…”
Section: Introductionmentioning
confidence: 99%
“…Use of oxides of pure Al 2 O 3 , TiO 2 , ZrO 2 , SiO 2 or their combinations for the preparation of ceramic membranes [5,[10][11][12][13][14][15][16][17][18][19][20][21][22][23][24][25][26] with high chemical, mechanical and thermal stabilities are well established [27,28] and are common, but the use of high cost inorganic precursors to obtain these oxides increases the cost as well as requires high sintering temperature (>1100 • C) for fabrication. The use of cheaper precursors such as ball clay, kaolin, quartz, feldspar, CaCO 3 , clay, sand and pyrophyllite for preparation of microfiltration range ceramic membranes have been reported [29,30].…”
Section: Introductionmentioning
confidence: 99%
“…Based on molecular size and shape, the rigid ceramic structure and precise tuning of the pore sizes endow inorganic membranes great capabilities for separation processes. For example, Singh et al [ 104 ] proposed cetyltrimethylammonium bromide (CTAB)—silica membrane with flat and hollow fiber polysulfone structure. At 25 °C, when 40 g/L NaCl seawater is pervaporated by the membrane and the salt resistance rate can reach 99.9%.…”
Section: Applications Of Polymeric Membranes For Pv Separationmentioning
confidence: 99%
“…Similar to the selection of membrane materials for gas dehydration processes [19], most membranes tested to date for PV desalination are based on hydrophilic materials to enhance the solubility component to water transport. Specifically, PV desalination studies were performed with polyether-polyamide block copolymer (PEBAX) [20][21][22], cellulose-based [23][24][25][26], polyvinyl alcohol-based (PVA) [27][28][29][30][31][32][33], graphene oxide (GO) [34][35][36], sulfonated block copolymers [37,38], ion-exchanged polyethylene [39], inorganic [40][41][42][43][44][45][46][47][48][49][50][51], and mixedmatrix/hybrid [32,[52][53][54][55]] active layers. For example, Li et al [35] synthesized a GO active layer on polyvinylidene fluoride (PVDF) support and reported a pure-water flux value of 67 kg m -² h -1 at 70 °C.…”
Section: Introductionmentioning
confidence: 99%