A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation

Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in t...
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Autor*in:	Fan, Huiqin [verfasserIn] Gao, Ailin [verfasserIn] Zhang, Guangfa [verfasserIn] Zhao, Shuai [verfasserIn] Cui, Jian [verfasserIn] Yan, Yehai [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2020

Schlagwörter:	Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection

Übergeordnetes Werk:	Enthalten in: Journal of membrane science - New York, NY [u.a.] : Elsevier, 1976, 602
Übergeordnetes Werk:	volume:602

DOI / URN:	10.1016/j.memsci.2020.117933

Katalog-ID:	ELV003870758

Internformat


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520			\|a Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS).
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650		4	\|a Surface wetting and fouling
650		4	\|a Salt rejection
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700	1		\|a Cui, Jian \|e verfasserin \|4 aut
700	1		\|a Yan, Yehai \|e verfasserin \|4 aut
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Indexfelder

author_variant	h f hf a g ag g z gz s z sz j c jc y y yy
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publishDate	2020
allfields	10.1016/j.memsci.2020.117933 doi (DE-627)ELV003870758 (ELSEVIER)S0376-7388(19)33320-4 DE-627 ger DE-627 rda eng 570 DE-600 58.11 bkl Fan, Huiqin verfasserin aut A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation 2020 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS). Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection Gao, Ailin verfasserin aut Zhang, Guangfa verfasserin aut Zhao, Shuai verfasserin aut Cui, Jian verfasserin aut Yan, Yehai verfasserin aut Enthalten in Journal of membrane science New York, NY [u.a.] : Elsevier, 1976 602 Online-Ressource (DE-627)302468927 (DE-600)1491419-0 (DE-576)259483907 0376-7388 nnns volume:602 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.11 Mechanische Verfahrenstechnik AR 602
spelling	10.1016/j.memsci.2020.117933 doi (DE-627)ELV003870758 (ELSEVIER)S0376-7388(19)33320-4 DE-627 ger DE-627 rda eng 570 DE-600 58.11 bkl Fan, Huiqin verfasserin aut A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation 2020 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS). Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection Gao, Ailin verfasserin aut Zhang, Guangfa verfasserin aut Zhao, Shuai verfasserin aut Cui, Jian verfasserin aut Yan, Yehai verfasserin aut Enthalten in Journal of membrane science New York, NY [u.a.] : Elsevier, 1976 602 Online-Ressource (DE-627)302468927 (DE-600)1491419-0 (DE-576)259483907 0376-7388 nnns volume:602 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.11 Mechanische Verfahrenstechnik AR 602
allfields_unstemmed	10.1016/j.memsci.2020.117933 doi (DE-627)ELV003870758 (ELSEVIER)S0376-7388(19)33320-4 DE-627 ger DE-627 rda eng 570 DE-600 58.11 bkl Fan, Huiqin verfasserin aut A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation 2020 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS). Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection Gao, Ailin verfasserin aut Zhang, Guangfa verfasserin aut Zhao, Shuai verfasserin aut Cui, Jian verfasserin aut Yan, Yehai verfasserin aut Enthalten in Journal of membrane science New York, NY [u.a.] : Elsevier, 1976 602 Online-Ressource (DE-627)302468927 (DE-600)1491419-0 (DE-576)259483907 0376-7388 nnns volume:602 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.11 Mechanische Verfahrenstechnik AR 602
allfieldsGer	10.1016/j.memsci.2020.117933 doi (DE-627)ELV003870758 (ELSEVIER)S0376-7388(19)33320-4 DE-627 ger DE-627 rda eng 570 DE-600 58.11 bkl Fan, Huiqin verfasserin aut A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation 2020 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS). Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection Gao, Ailin verfasserin aut Zhang, Guangfa verfasserin aut Zhao, Shuai verfasserin aut Cui, Jian verfasserin aut Yan, Yehai verfasserin aut Enthalten in Journal of membrane science New York, NY [u.a.] : Elsevier, 1976 602 Online-Ressource (DE-627)302468927 (DE-600)1491419-0 (DE-576)259483907 0376-7388 nnns volume:602 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.11 Mechanische Verfahrenstechnik AR 602
allfieldsSound	10.1016/j.memsci.2020.117933 doi (DE-627)ELV003870758 (ELSEVIER)S0376-7388(19)33320-4 DE-627 ger DE-627 rda eng 570 DE-600 58.11 bkl Fan, Huiqin verfasserin aut A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation 2020 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS). Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection Gao, Ailin verfasserin aut Zhang, Guangfa verfasserin aut Zhao, Shuai verfasserin aut Cui, Jian verfasserin aut Yan, Yehai verfasserin aut Enthalten in Journal of membrane science New York, NY [u.a.] : Elsevier, 1976 602 Online-Ressource (DE-627)302468927 (DE-600)1491419-0 (DE-576)259483907 0376-7388 nnns volume:602 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 58.11 Mechanische Verfahrenstechnik AR 602
language	English
source	Enthalten in Journal of membrane science 602 volume:602
sourceStr	Enthalten in Journal of membrane science 602 volume:602
format_phy_str_mv	Article
bklname	Mechanische Verfahrenstechnik
institution	findex.gbv.de
topic_facet	Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection
dewey-raw	570
isfreeaccess_bool	false
container_title	Journal of membrane science
authorswithroles_txt_mv	Fan, Huiqin @@aut@@ Gao, Ailin @@aut@@ Zhang, Guangfa @@aut@@ Zhao, Shuai @@aut@@ Cui, Jian @@aut@@ Yan, Yehai @@aut@@
publishDateDaySort_date	2020-01-01T00:00:00Z
hierarchy_top_id	302468927
dewey-sort	3570
id	ELV003870758
language_de	englisch
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author	Fan, Huiqin
spellingShingle	Fan, Huiqin ddc 570 bkl 58.11 misc Amphiphobic membrane misc Double re-entrant structure misc Membrane distillation misc Surface wetting and fouling misc Salt rejection A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation
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topic_title	570 DE-600 58.11 bkl A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation Amphiphobic membrane Double re-entrant structure Membrane distillation Surface wetting and fouling Salt rejection
topic	ddc 570 bkl 58.11 misc Amphiphobic membrane misc Double re-entrant structure misc Membrane distillation misc Surface wetting and fouling misc Salt rejection
topic_unstemmed	ddc 570 bkl 58.11 misc Amphiphobic membrane misc Double re-entrant structure misc Membrane distillation misc Surface wetting and fouling misc Salt rejection
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title	A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation
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title_full	A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation
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title_sort	a facile strategy towards developing amphiphobic polysulfone membrane with double re-entrant structure for membrane distillation
title_auth	A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation
abstract	Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS).
abstractGer	Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS).
abstract_unstemmed	Membrane surface wetting and fouling are still crucial issues in many separation processes such as membrane distillation (MD), especially when oil-contained feed solution was treated. To solve that problem, a facile synthesis strategy for amphiphobic polymeric membrane was successfully proposed in the current work. Via traditional non-solvent induced phase separation (NIPS) and subsequent sol-gel process, double re-entrant structure was ingeniously constructed; that is, the first level re-entrant structure was supplied by the bicontinuous inter-connected porous structure obtained through optimized phase separation parameters and the second level re-entrant structure was offered by the spherical and dimensionally different silicon dioxide (SiO2) nanoparticles which were spontaneously generated during sol-gel process. After cooperating with the fluorine-contained chemical coating, the resultant polysulfone (PSf) membrane with double re-entrant structure exhibited excellent and stable repellency performance to both water and organic liquid, even showing high hexadecane contact angle of 121° and hexane of 67°. Compared with solely hydrophobic membrane, the as-fabricated amphiphobic PSf membrane achieved long-term stable vapor flux and salt rejection in MD process even with the presence of surfactant sodium dodecyl sulfonate (SDS).
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title_short	A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation
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author2	Gao, Ailin Zhang, Guangfa Zhao, Shuai Cui, Jian Yan, Yehai
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A facile strategy towards developing amphiphobic polysulfone membrane with double Re-entrant structure for membrane distillation

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