Thin film composite hollow fiber membrane for separation in biorefinery

One of the newest applications of the membrane technology is for the separation of sugar component and inhibitor removal during biomass processing in biorefinery. Most of the membranes used in biorefinery were commercially purchased and not specifically customise for the biomass hydrolysate processi...

Full description

Saved in:
Bibliographic Details
Main Authors: Anuar, E., Saufi, S. M., Seman, M. N. A., Yussof, H. W., Ismailb, A. F.
Format: Article
Published: Italian Association of Chemical Engineering - AIDIC 2017
Subjects:
Online Access:http://eprints.utm.my/id/eprint/75579/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85019411989&doi=10.3303%2fCET1756184&partnerID=40&md5=6bf2172e4b9a89cf5614fac648b8f3d8
Tags: Add Tag
No Tags, Be the first to tag this record!
id my.utm.75579
record_format eprints
spelling my.utm.755792018-04-15T08:05:30Z http://eprints.utm.my/id/eprint/75579/ Thin film composite hollow fiber membrane for separation in biorefinery Anuar, E. Saufi, S. M. Seman, M. N. A. Yussof, H. W. Ismailb, A. F. TP Chemical technology One of the newest applications of the membrane technology is for the separation of sugar component and inhibitor removal during biomass processing in biorefinery. Most of the membranes used in biorefinery were commercially purchased and not specifically customise for the biomass hydrolysate processing. In the current study, a series of thin film composite (TFC) hollow fiber membranes were fabricated to tailor the performance toward xylose/glucose refinement and acetic acid removal in biomass processing. Polysulfone (PSf) hollow fiber membrane support was prepared using 20 wt% PSf, 2 wt% polyvinylpyrrolidone K30 (PVP K30) and 78 wt% dimethylformamide (DMF) through dry/wet spinning process. Three types of aqueous monomers were studied in interfacial polymerisation process, which are piperazine (PIP), triethanolamine (TEOA) and polyethyleneimine (PEI). TFC hollow fiber membrane prepared using TEOA monomer showed the best performance for separation of biomass hydrolysate component. It exhibited rejection value 50.98 ± 4.11 % of xylose, 71.72 ± 3.92 % of glucose and 5.45 ± 1.93 % of acetic acid. This is corresponding to the ideal separation factor of 1.75 ± 0.10 for xylose/glucose, 3.42 ± 0.54 for acetic acid/glucose and 1.95 ± 0.20 for acetic acid/xylose. Italian Association of Chemical Engineering - AIDIC 2017 Article PeerReviewed Anuar, E. and Saufi, S. M. and Seman, M. N. A. and Yussof, H. W. and Ismailb, A. F. (2017) Thin film composite hollow fiber membrane for separation in biorefinery. Chemical Engineering Transactions, 56 . pp. 1099-1104. ISSN 2283-9216 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85019411989&doi=10.3303%2fCET1756184&partnerID=40&md5=6bf2172e4b9a89cf5614fac648b8f3d8
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
Anuar, E.
Saufi, S. M.
Seman, M. N. A.
Yussof, H. W.
Ismailb, A. F.
Thin film composite hollow fiber membrane for separation in biorefinery
description One of the newest applications of the membrane technology is for the separation of sugar component and inhibitor removal during biomass processing in biorefinery. Most of the membranes used in biorefinery were commercially purchased and not specifically customise for the biomass hydrolysate processing. In the current study, a series of thin film composite (TFC) hollow fiber membranes were fabricated to tailor the performance toward xylose/glucose refinement and acetic acid removal in biomass processing. Polysulfone (PSf) hollow fiber membrane support was prepared using 20 wt% PSf, 2 wt% polyvinylpyrrolidone K30 (PVP K30) and 78 wt% dimethylformamide (DMF) through dry/wet spinning process. Three types of aqueous monomers were studied in interfacial polymerisation process, which are piperazine (PIP), triethanolamine (TEOA) and polyethyleneimine (PEI). TFC hollow fiber membrane prepared using TEOA monomer showed the best performance for separation of biomass hydrolysate component. It exhibited rejection value 50.98 ± 4.11 % of xylose, 71.72 ± 3.92 % of glucose and 5.45 ± 1.93 % of acetic acid. This is corresponding to the ideal separation factor of 1.75 ± 0.10 for xylose/glucose, 3.42 ± 0.54 for acetic acid/glucose and 1.95 ± 0.20 for acetic acid/xylose.
format Article
author Anuar, E.
Saufi, S. M.
Seman, M. N. A.
Yussof, H. W.
Ismailb, A. F.
author_facet Anuar, E.
Saufi, S. M.
Seman, M. N. A.
Yussof, H. W.
Ismailb, A. F.
author_sort Anuar, E.
title Thin film composite hollow fiber membrane for separation in biorefinery
title_short Thin film composite hollow fiber membrane for separation in biorefinery
title_full Thin film composite hollow fiber membrane for separation in biorefinery
title_fullStr Thin film composite hollow fiber membrane for separation in biorefinery
title_full_unstemmed Thin film composite hollow fiber membrane for separation in biorefinery
title_sort thin film composite hollow fiber membrane for separation in biorefinery
publisher Italian Association of Chemical Engineering - AIDIC
publishDate 2017
url http://eprints.utm.my/id/eprint/75579/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85019411989&doi=10.3303%2fCET1756184&partnerID=40&md5=6bf2172e4b9a89cf5614fac648b8f3d8
_version_ 1643657101473480704
score 13.211869