New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal

Interfacial polymerization of a thin film composite (TFC) layer on top of a miroporous support membrane or other porous substrate is one of adequate method to form nanofiltration membrane in order to remove humic acid. Ultrafiltration (UF) polyethersulfone (PES) was used as membrane base support. Re...

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Main Authors: Nurul Ain , Jalanni, Mazrul Nizam, Abu Seman, C. K. M., Faizal
Format: Article
Language:English
Published: Trans Tech Publications, Switzerland 2015
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Online Access:http://umpir.ump.edu.my/id/eprint/10050/1/New%20Polyester%20Nanofiltration%20%28NF%29%20Membrane%20for%20Humic%20Acid%20Removal.pdf
http://umpir.ump.edu.my/id/eprint/10050/
http://www.scientific.net/AMR.1107.383
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spelling my.ump.umpir.100502018-01-12T03:27:24Z http://umpir.ump.edu.my/id/eprint/10050/ New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal Nurul Ain , Jalanni Mazrul Nizam, Abu Seman C. K. M., Faizal TP Chemical technology Interfacial polymerization of a thin film composite (TFC) layer on top of a miroporous support membrane or other porous substrate is one of adequate method to form nanofiltration membrane in order to remove humic acid. Ultrafiltration (UF) polyethersulfone (PES) was used as membrane base support. Reaction occurred on the surface of membrane between two phase which are triethanolamine (TEOA) and trimesoyl chloride (TMC) as aqueous solution and organic solution respectively. Membrane that produced characterized by permeability, charged solutes rejection including salt solutions (NaCl and Na2SO4) and humic acid removal. Properties of membrane can be attributed with the changes of monomer concentration and reaction time. Pure water flux Jw for membranes calculated as a function of applied pressure to membrane ΔP. Thus, flux increased linearly with operating pressure is applied to membrane where meets Hagen-Poiseuille equation and gradient of every straight line give pure water permeability data. The variation of reaction time (15, 25 and 35 min) at 8% (w/v) monomer concentrations can affect the properties of the membrane produced and decreasing water permeabilities. The rejection order of the membrane changed from 0.001 M Na2SO4 > 0.1M Na2SO4> 0.001M NaCl > 0.1M NaCl. Humic acid removal resulted almost fully rejection showed that nanofiltration membrane is one of the best methods in water treatment technology. Trans Tech Publications, Switzerland 2015 Article PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/10050/1/New%20Polyester%20Nanofiltration%20%28NF%29%20Membrane%20for%20Humic%20Acid%20Removal.pdf Nurul Ain , Jalanni and Mazrul Nizam, Abu Seman and C. K. M., Faizal (2015) New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal. Advanced Materials Research, 1107. pp. 383-388. ISSN 1022-6680 (print), 1662-8985 (online) http://www.scientific.net/AMR.1107.383 DOI: 10.4028/www.scientific.net/AMR.1107.383
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Nurul Ain , Jalanni
Mazrul Nizam, Abu Seman
C. K. M., Faizal
New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal
description Interfacial polymerization of a thin film composite (TFC) layer on top of a miroporous support membrane or other porous substrate is one of adequate method to form nanofiltration membrane in order to remove humic acid. Ultrafiltration (UF) polyethersulfone (PES) was used as membrane base support. Reaction occurred on the surface of membrane between two phase which are triethanolamine (TEOA) and trimesoyl chloride (TMC) as aqueous solution and organic solution respectively. Membrane that produced characterized by permeability, charged solutes rejection including salt solutions (NaCl and Na2SO4) and humic acid removal. Properties of membrane can be attributed with the changes of monomer concentration and reaction time. Pure water flux Jw for membranes calculated as a function of applied pressure to membrane ΔP. Thus, flux increased linearly with operating pressure is applied to membrane where meets Hagen-Poiseuille equation and gradient of every straight line give pure water permeability data. The variation of reaction time (15, 25 and 35 min) at 8% (w/v) monomer concentrations can affect the properties of the membrane produced and decreasing water permeabilities. The rejection order of the membrane changed from 0.001 M Na2SO4 > 0.1M Na2SO4> 0.001M NaCl > 0.1M NaCl. Humic acid removal resulted almost fully rejection showed that nanofiltration membrane is one of the best methods in water treatment technology.
format Article
author Nurul Ain , Jalanni
Mazrul Nizam, Abu Seman
C. K. M., Faizal
author_facet Nurul Ain , Jalanni
Mazrul Nizam, Abu Seman
C. K. M., Faizal
author_sort Nurul Ain , Jalanni
title New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal
title_short New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal
title_full New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal
title_fullStr New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal
title_full_unstemmed New Polyester Nanofiltration (NF) Membrane for Humic Acid Removal
title_sort new polyester nanofiltration (nf) membrane for humic acid removal
publisher Trans Tech Publications, Switzerland
publishDate 2015
url http://umpir.ump.edu.my/id/eprint/10050/1/New%20Polyester%20Nanofiltration%20%28NF%29%20Membrane%20for%20Humic%20Acid%20Removal.pdf
http://umpir.ump.edu.my/id/eprint/10050/
http://www.scientific.net/AMR.1107.383
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score 13.15806