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Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application

Shaheen Fatima Anis, Boor Singh Lalia, Raed Hashaikeh, Nidal Hilal

Separation and Purification Technology, Volume: 242, Start page: 116824

Swansea University Author: Nidal Hilal

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DOI (Published version): 10.1016/j.seppur.2020.116824

Abstract

Membrane performance is a region of growing research interest, where new functional nanomaterials are continually sought. In this study, nano zeolite type Y was prepared through a unique ball milling process. The produced zeolite has a high surface area, and abundant flow channels with a well-define...

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Published in: Separation and Purification Technology
ISSN: 1383-5866
Published: Elsevier BV 2020
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URI: https://cronfa.swan.ac.uk/Record/cronfa53749
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spelling 2021-03-15T12:52:02.5231974 v2 53749 2020-03-07 Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application 3acba771241d878c8e35ff464aec0342 Nidal Hilal Nidal Hilal true false 2020-03-07 FGSEN Membrane performance is a region of growing research interest, where new functional nanomaterials are continually sought. In this study, nano zeolite type Y was prepared through a unique ball milling process. The produced zeolite has a high surface area, and abundant flow channels with a well-defined pore structure facilitating water passage, but at the same time restricting the passage of contaminants through the molecular sieving effect. Polysulfone (PSf) membranes were prepared through phase inversion with nano-Y loadings from 0.2 to 1.5 wt. %. Membranes were characterized for their structure, morphology, thermal stability and porosity. The developed membranes were tested for micellar enhanced ultrafiltration (MEUF) cationic dye rejections. The addition of nano-Y zeolite affected both the flux and dye rejection of the membranes. Optimum performance was obtained at 0.4 wt. % nano-Y loading, giving a rejection of 99.5% and a corresponding flux of 105 L.m-2.h-1. The static contact angle measurements indicate that membrane hydrophilicity increased with progressive nano-Y additions until 0.4 wt. %, after which the membrane showed no further change in hydrophilic character. The obtained effects of nano-Y addition on membrane performance was attributed to the well-connected 3-D microporous structure in which nano-Y zeolite provided preferential water pathways though nanoporous hydrophilic channels. Whereas, the high dye rejection was attributed to the fact that nano-Y zeolite is negatively charged and, as a result, provided resistance to the negatively charged micelles, and further restricted its passage through the microporous zeolite structure. Journal Article Separation and Purification Technology 242 116824 Elsevier BV 1383-5866 Ultrafiltration, micellar, nano-zeolite, dye rejection, phase inversion 1 7 2020 2020-07-01 10.1016/j.seppur.2020.116824 COLLEGE NANME Science and Engineering - Faculty COLLEGE CODE FGSEN Swansea University 2021-03-15T12:52:02.5231974 2020-03-07T04:47:40.2783939 Professional Services ISS - Uncategorised Shaheen Fatima Anis 1 Boor Singh Lalia 2 Raed Hashaikeh 3 Nidal Hilal 4 53749__16841__e9885402480b4607b7e8089ea9d302d4.pdf anis2020.pdf 2020-03-12T14:04:27.1034620 Output 9624314 application/pdf Accepted Manuscript true 2021-03-09T00:00:00.0000000 Released under the terms of a Creative Commons Attribution Non-Commercial No Derivatives License (CC-BY-NC-ND). true eng http://creativecommons.org/licenses/by-nc-nd/4.0/
title Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application
spellingShingle Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application
Nidal Hilal
title_short Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application
title_full Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application
title_fullStr Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application
title_full_unstemmed Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application
title_sort Breaking through the selectivity-permeability tradeoff using nano zeolite-Y for micellar enhanced ultrafiltration dye rejection application
author_id_str_mv 3acba771241d878c8e35ff464aec0342
author_id_fullname_str_mv 3acba771241d878c8e35ff464aec0342_***_Nidal Hilal
author Nidal Hilal
author2 Shaheen Fatima Anis
Boor Singh Lalia
Raed Hashaikeh
Nidal Hilal
format Journal article
container_title Separation and Purification Technology
container_volume 242
container_start_page 116824
publishDate 2020
institution Swansea University
issn 1383-5866
doi_str_mv 10.1016/j.seppur.2020.116824
publisher Elsevier BV
college_str Professional Services
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hierarchy_top_id professionalservices
hierarchy_top_title Professional Services
hierarchy_parent_id professionalservices
hierarchy_parent_title Professional Services
department_str ISS - Uncategorised{{{_:::_}}}Professional Services{{{_:::_}}}ISS - Uncategorised
document_store_str 1
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description Membrane performance is a region of growing research interest, where new functional nanomaterials are continually sought. In this study, nano zeolite type Y was prepared through a unique ball milling process. The produced zeolite has a high surface area, and abundant flow channels with a well-defined pore structure facilitating water passage, but at the same time restricting the passage of contaminants through the molecular sieving effect. Polysulfone (PSf) membranes were prepared through phase inversion with nano-Y loadings from 0.2 to 1.5 wt. %. Membranes were characterized for their structure, morphology, thermal stability and porosity. The developed membranes were tested for micellar enhanced ultrafiltration (MEUF) cationic dye rejections. The addition of nano-Y zeolite affected both the flux and dye rejection of the membranes. Optimum performance was obtained at 0.4 wt. % nano-Y loading, giving a rejection of 99.5% and a corresponding flux of 105 L.m-2.h-1. The static contact angle measurements indicate that membrane hydrophilicity increased with progressive nano-Y additions until 0.4 wt. %, after which the membrane showed no further change in hydrophilic character. The obtained effects of nano-Y addition on membrane performance was attributed to the well-connected 3-D microporous structure in which nano-Y zeolite provided preferential water pathways though nanoporous hydrophilic channels. Whereas, the high dye rejection was attributed to the fact that nano-Y zeolite is negatively charged and, as a result, provided resistance to the negatively charged micelles, and further restricted its passage through the microporous zeolite structure.
published_date 2020-07-01T04:06:52Z
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score 11.013171

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