Porous polyether sulfone for direct methanol fuel cell applications: structural analysis

Porous poly ether sulfone (PES) membranes were prepared using two different solvents which were N-methyl-2-pyrrolidone and dimethylacetamide (DMAc) via dry/wet non-solvent phase inversion (NIPS) techniques. PES with the compositions of 18 wt% is prepared for each dope solution. During the membrane c...

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Main Authors: Junoh, Hazlina, Jaafar, Juhana, M. Nordin, Nik Abdul Hadi, Ismail, Ahmad F., Othman, Mohd. H. D., A. Rahman, Mukhlis, Aziz, Farhana, Yusof, Norhaniza, Sayed Daud, Syarifah Noor S.
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Published: John Wiley and Sons Ltd 2021
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Online Access:http://eprints.utm.my/id/eprint/91743/
http://dx.doi.org/10.1002/er.5921
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spelling my.utm.917432021-07-28T08:42:25Z http://eprints.utm.my/id/eprint/91743/ Porous polyether sulfone for direct methanol fuel cell applications: structural analysis Junoh, Hazlina Jaafar, Juhana M. Nordin, Nik Abdul Hadi Ismail, Ahmad F. Othman, Mohd. H. D. A. Rahman, Mukhlis Aziz, Farhana Yusof, Norhaniza Sayed Daud, Syarifah Noor S. TP Chemical technology Porous poly ether sulfone (PES) membranes were prepared using two different solvents which were N-methyl-2-pyrrolidone and dimethylacetamide (DMAc) via dry/wet non-solvent phase inversion (NIPS) techniques. PES with the compositions of 18 wt% is prepared for each dope solution. During the membrane casting process, 0 to 5 minutes delay prior to immersion in coagulant bath is set in order to allow solvent evaporation to take place. Water is used as the non-solvent for solvent exchange process. The prepared membranes are characterised based on their morphological aspect using scanning electron microscopy towards the effect of solvent evaporation time and solution viscosity. The changes in proton conductivity, methanol permeability, water uptake and hydrophilicity/hydrophobicity behaviours are also studied. Conclusively, the 18 wt% PES membranes prepared with DMAc as solvent at 3 minutes solvent evaporation time exhibited desirable pore size for proton conduction (0.04 × 10−3 Scm−1) and methanol resistant effect that consequently contribute to considerably low methanol permeability rate at 0.06 × 10−7 cm2 s−1 which could elevate the direct methanol fuel cell performance. John Wiley and Sons Ltd 2021-02 Article PeerReviewed Junoh, Hazlina and Jaafar, Juhana and M. Nordin, Nik Abdul Hadi and Ismail, Ahmad F. and Othman, Mohd. H. D. and A. Rahman, Mukhlis and Aziz, Farhana and Yusof, Norhaniza and Sayed Daud, Syarifah Noor S. (2021) Porous polyether sulfone for direct methanol fuel cell applications: structural analysis. International Journal of Energy Research, 45 (2). pp. 2277-2291. ISSN 0363-907X http://dx.doi.org/10.1002/er.5921 DOI:10.1002/er.5921
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 TP Chemical technology
spellingShingle TP Chemical technology
Junoh, Hazlina
Jaafar, Juhana
M. Nordin, Nik Abdul Hadi
Ismail, Ahmad F.
Othman, Mohd. H. D.
A. Rahman, Mukhlis
Aziz, Farhana
Yusof, Norhaniza
Sayed Daud, Syarifah Noor S.
Porous polyether sulfone for direct methanol fuel cell applications: structural analysis
description Porous poly ether sulfone (PES) membranes were prepared using two different solvents which were N-methyl-2-pyrrolidone and dimethylacetamide (DMAc) via dry/wet non-solvent phase inversion (NIPS) techniques. PES with the compositions of 18 wt% is prepared for each dope solution. During the membrane casting process, 0 to 5 minutes delay prior to immersion in coagulant bath is set in order to allow solvent evaporation to take place. Water is used as the non-solvent for solvent exchange process. The prepared membranes are characterised based on their morphological aspect using scanning electron microscopy towards the effect of solvent evaporation time and solution viscosity. The changes in proton conductivity, methanol permeability, water uptake and hydrophilicity/hydrophobicity behaviours are also studied. Conclusively, the 18 wt% PES membranes prepared with DMAc as solvent at 3 minutes solvent evaporation time exhibited desirable pore size for proton conduction (0.04 × 10−3 Scm−1) and methanol resistant effect that consequently contribute to considerably low methanol permeability rate at 0.06 × 10−7 cm2 s−1 which could elevate the direct methanol fuel cell performance.
format Article
author Junoh, Hazlina
Jaafar, Juhana
M. Nordin, Nik Abdul Hadi
Ismail, Ahmad F.
Othman, Mohd. H. D.
A. Rahman, Mukhlis
Aziz, Farhana
Yusof, Norhaniza
Sayed Daud, Syarifah Noor S.
author_facet Junoh, Hazlina
Jaafar, Juhana
M. Nordin, Nik Abdul Hadi
Ismail, Ahmad F.
Othman, Mohd. H. D.
A. Rahman, Mukhlis
Aziz, Farhana
Yusof, Norhaniza
Sayed Daud, Syarifah Noor S.
author_sort Junoh, Hazlina
title Porous polyether sulfone for direct methanol fuel cell applications: structural analysis
title_short Porous polyether sulfone for direct methanol fuel cell applications: structural analysis
title_full Porous polyether sulfone for direct methanol fuel cell applications: structural analysis
title_fullStr Porous polyether sulfone for direct methanol fuel cell applications: structural analysis
title_full_unstemmed Porous polyether sulfone for direct methanol fuel cell applications: structural analysis
title_sort porous polyether sulfone for direct methanol fuel cell applications: structural analysis
publisher John Wiley and Sons Ltd
publishDate 2021
url http://eprints.utm.my/id/eprint/91743/
http://dx.doi.org/10.1002/er.5921
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