Cargando…

Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation

Hydrophobic pure-silica *BEA-type zeolite membranes with large pores were prepared on tubular silica supports by hydrothermal synthesis using a secondary growth method and were applied to the separation of alcohol/water mixtures by pervaporation (PV), an alternative energy-efficient process for prod...

Descripción completa

Detalles Bibliográficos
Autores principales: Ueno, Kyohei, Yamada, Saki, Watanabe, Toshinari, Negishi, Hideyuki, Okuno, Takuya, Tawarayama, Hiromasa, Ishikawa, Shinji, Miyamoto, Manabu, Uemiya, Shigeyuki, Oumi, Yasunori
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6680943/
https://www.ncbi.nlm.nih.gov/pubmed/31319501
http://dx.doi.org/10.3390/membranes9070086
_version_ 1783441618068570112
author Ueno, Kyohei
Yamada, Saki
Watanabe, Toshinari
Negishi, Hideyuki
Okuno, Takuya
Tawarayama, Hiromasa
Ishikawa, Shinji
Miyamoto, Manabu
Uemiya, Shigeyuki
Oumi, Yasunori
author_facet Ueno, Kyohei
Yamada, Saki
Watanabe, Toshinari
Negishi, Hideyuki
Okuno, Takuya
Tawarayama, Hiromasa
Ishikawa, Shinji
Miyamoto, Manabu
Uemiya, Shigeyuki
Oumi, Yasunori
author_sort Ueno, Kyohei
collection PubMed
description Hydrophobic pure-silica *BEA-type zeolite membranes with large pores were prepared on tubular silica supports by hydrothermal synthesis using a secondary growth method and were applied to the separation of alcohol/water mixtures by pervaporation (PV), an alternative energy-efficient process for production of biofuels. Amorphous pure-silica tubular silica supports, free of Al atoms, were used for preparing the membranes. In this study, the effects of the synthesis conditions, such as the H(2)O/SiO(2) and NH(4)F/SiO(2) ratios in the synthetic gel, on the membrane formation process and separation performance were systematically investigated. The successfully prepared dense and continuous membranes exhibited alcohol selectivity and high flux for the separation of ethanol/water and butanol/water mixtures. The pure-silica *BEA membranes obtained under optimal conditions (0.08SiO(2):0.5TEAOH:0.7NH(4)F:8H(2)O) showed high PV performance with a separation factor of 229 and a flux of 0.62 kg·m(−2)·h(−1) for a 1 wt % n-butanol/water mixture at 318 K. This result was attributed to the hydrophobicity and large pore size of the pure-silica *BEA membrane. This was the first successful synthesis of hydrophobic large-pore zeolite membranes on tubular supports with alcohol selectivity, and the obtained results could provide new insights into the research on hydrophobic membranes with high permeability.
format Online
Article
Text
id pubmed-6680943
institution National Center for Biotechnology Information
language English
publishDate 2019
publisher MDPI
record_format MEDLINE/PubMed
spelling pubmed-66809432019-08-09 Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation Ueno, Kyohei Yamada, Saki Watanabe, Toshinari Negishi, Hideyuki Okuno, Takuya Tawarayama, Hiromasa Ishikawa, Shinji Miyamoto, Manabu Uemiya, Shigeyuki Oumi, Yasunori Membranes (Basel) Article Hydrophobic pure-silica *BEA-type zeolite membranes with large pores were prepared on tubular silica supports by hydrothermal synthesis using a secondary growth method and were applied to the separation of alcohol/water mixtures by pervaporation (PV), an alternative energy-efficient process for production of biofuels. Amorphous pure-silica tubular silica supports, free of Al atoms, were used for preparing the membranes. In this study, the effects of the synthesis conditions, such as the H(2)O/SiO(2) and NH(4)F/SiO(2) ratios in the synthetic gel, on the membrane formation process and separation performance were systematically investigated. The successfully prepared dense and continuous membranes exhibited alcohol selectivity and high flux for the separation of ethanol/water and butanol/water mixtures. The pure-silica *BEA membranes obtained under optimal conditions (0.08SiO(2):0.5TEAOH:0.7NH(4)F:8H(2)O) showed high PV performance with a separation factor of 229 and a flux of 0.62 kg·m(−2)·h(−1) for a 1 wt % n-butanol/water mixture at 318 K. This result was attributed to the hydrophobicity and large pore size of the pure-silica *BEA membrane. This was the first successful synthesis of hydrophobic large-pore zeolite membranes on tubular supports with alcohol selectivity, and the obtained results could provide new insights into the research on hydrophobic membranes with high permeability. MDPI 2019-07-17 /pmc/articles/PMC6680943/ /pubmed/31319501 http://dx.doi.org/10.3390/membranes9070086 Text en © 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Ueno, Kyohei
Yamada, Saki
Watanabe, Toshinari
Negishi, Hideyuki
Okuno, Takuya
Tawarayama, Hiromasa
Ishikawa, Shinji
Miyamoto, Manabu
Uemiya, Shigeyuki
Oumi, Yasunori
Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation
title Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation
title_full Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation
title_fullStr Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation
title_full_unstemmed Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation
title_short Hydrophobic *BEA-Type Zeolite Membranes on Tubular Silica Supports for Alcohol/Water Separation by Pervaporation
title_sort hydrophobic *bea-type zeolite membranes on tubular silica supports for alcohol/water separation by pervaporation
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6680943/
https://www.ncbi.nlm.nih.gov/pubmed/31319501
http://dx.doi.org/10.3390/membranes9070086
work_keys_str_mv AT uenokyohei hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT yamadasaki hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT watanabetoshinari hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT negishihideyuki hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT okunotakuya hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT tawarayamahiromasa hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT ishikawashinji hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT miyamotomanabu hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT uemiyashigeyuki hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation
AT oumiyasunori hydrophobicbeatypezeolitemembranesontubularsilicasupportsforalcoholwaterseparationbypervaporation