High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane

Novel mixed matrix membranes were prepared from polysulfone (PSf), talc and Fe3O4–talc nanocomposite by phase inversion technique. PSf/Fe3O4–talc membranes showed higher lead and nickel rejections compared to PSf/talc membranes, which reaches to 99.4 and 96.2% for lead and nickel ions, respectively,...

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Main Authors: Moradihamedani, P., Kalantari, K., Abdullah, A. H., Morad, N. A.
Format: Article
Published: Taylor and Francis Inc. 2016
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Online Access:http://eprints.utm.my/id/eprint/71512/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84975215490&doi=10.1080%2f19443994.2016.1193449&partnerID=40&md5=61efe631c90b836d6ae5299ece48b956
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Institution: Universiti Teknologi Malaysia
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spelling my.utm.715122017-11-15T03:36:01Z http://eprints.utm.my/id/eprint/71512/ High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane Moradihamedani, P. Kalantari, K. Abdullah, A. H. Morad, N. A. T Technology (General) Novel mixed matrix membranes were prepared from polysulfone (PSf), talc and Fe3O4–talc nanocomposite by phase inversion technique. PSf/Fe3O4–talc membranes showed higher lead and nickel rejections compared to PSf/talc membranes, which reaches to 99.4 and 96.2% for lead and nickel ions, respectively, at feed pH 5 and lower rejections at pH 3.5 and 2. Higher surface area in Fe3O4–talc nanocomposite than talc could be considered as a main reason of higher heavy metals removal in PSf/Fe3O4–talc membranes. The heavy metals removal enhances with the increase in nanocomposite content from 7 to 9 wt.% because higher numbers of vacant sites in membrane morphology were available for adsorption. Heavy metals rejection reduces in higher nanocomposite concentrations (11 and 13 wt.%) due to the formation of macrovoids in membrane substructure. In addition, a reduction in the metal ion rejection was recognized by enhancement in feed solution concentration and applied pressure. This is caused by difficulty for the remaining vacant sites to be filled with the heavy metal ions because of repulsive forces between the adsorbed solute molecules on the surface and solute in bulk phase. The interactions of lead and nickel ions with nanocomposite placed on the membrane top layer were revealed by the scanning electron microscopy with energy dispersive X-rays. Taylor and Francis Inc. 2016 Article PeerReviewed Moradihamedani, P. and Kalantari, K. and Abdullah, A. H. and Morad, N. A. (2016) High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane. Desalination and Water Treatment, 57 (59). pp. 28900-28909. ISSN 1944-3994 https://www.scopus.com/inward/record.uri?eid=2-s2.0-84975215490&doi=10.1080%2f19443994.2016.1193449&partnerID=40&md5=61efe631c90b836d6ae5299ece48b956
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
topic T Technology (General)
spellingShingle T Technology (General)
Moradihamedani, P.
Kalantari, K.
Abdullah, A. H.
Morad, N. A.
High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane
description Novel mixed matrix membranes were prepared from polysulfone (PSf), talc and Fe3O4–talc nanocomposite by phase inversion technique. PSf/Fe3O4–talc membranes showed higher lead and nickel rejections compared to PSf/talc membranes, which reaches to 99.4 and 96.2% for lead and nickel ions, respectively, at feed pH 5 and lower rejections at pH 3.5 and 2. Higher surface area in Fe3O4–talc nanocomposite than talc could be considered as a main reason of higher heavy metals removal in PSf/Fe3O4–talc membranes. The heavy metals removal enhances with the increase in nanocomposite content from 7 to 9 wt.% because higher numbers of vacant sites in membrane morphology were available for adsorption. Heavy metals rejection reduces in higher nanocomposite concentrations (11 and 13 wt.%) due to the formation of macrovoids in membrane substructure. In addition, a reduction in the metal ion rejection was recognized by enhancement in feed solution concentration and applied pressure. This is caused by difficulty for the remaining vacant sites to be filled with the heavy metal ions because of repulsive forces between the adsorbed solute molecules on the surface and solute in bulk phase. The interactions of lead and nickel ions with nanocomposite placed on the membrane top layer were revealed by the scanning electron microscopy with energy dispersive X-rays.
format Article
author Moradihamedani, P.
Kalantari, K.
Abdullah, A. H.
Morad, N. A.
author_facet Moradihamedani, P.
Kalantari, K.
Abdullah, A. H.
Morad, N. A.
author_sort Moradihamedani, P.
title High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane
title_short High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane
title_full High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane
title_fullStr High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane
title_full_unstemmed High efficient removal of lead(II) and nickel(II) from aqueous solution by novel polysulfone/Fe3O4–talc nanocomposite mixed matrix membrane
title_sort high efficient removal of lead(ii) and nickel(ii) from aqueous solution by novel polysulfone/fe3o4–talc nanocomposite mixed matrix membrane
publisher Taylor and Francis Inc.
publishDate 2016
url http://eprints.utm.my/id/eprint/71512/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84975215490&doi=10.1080%2f19443994.2016.1193449&partnerID=40&md5=61efe631c90b836d6ae5299ece48b956
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