Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model

The incorporation of highly selective molecular sieve such as carbon molecular sieve (CMS) and highly affinitive solvent such as diethanolamine (DEA) into polyethersulfone (PES) have been implemented to synthesize amine mixed matrix membranes (MMMs) with an enhanced gas performance. Synergetic effec...

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Main Authors: Nasir, R., Mukhtar, H., Man, Z.
Format: Article
Published: Royal Society of Chemistry 2016
Online Access:http://scholars.utp.edu.my/id/eprint/22060/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84978602346&doi=10.1039%2fc5ra27756f&partnerID=40&md5=0d0cd0774ca866c357b8f82f95aed43e
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spelling oai:scholars.utp.edu.my:220602023-04-11T04:14:37Z http://scholars.utp.edu.my/id/eprint/22060/ Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model Nasir, R. Mukhtar, H. Man, Z. The incorporation of highly selective molecular sieve such as carbon molecular sieve (CMS) and highly affinitive solvent such as diethanolamine (DEA) into polyethersulfone (PES) have been implemented to synthesize amine mixed matrix membranes (MMMs) with an enhanced gas performance. Synergetic effect of CMS and DEA has caused the improvement of carbon dioxide (CO2) permeability and ideal CO2/CH4 selectivity. While existing theoretical models define the relative permeability well for binary mixed matrix membranes they fail to predict the relative permeability of amine mixed matrix membranes. In fact, the degree of deviation from the simple model predictions provides understanding into the detailed properties of the third component, which has been neglected in previous analyses of these models. Modification of an existing model, namely the Maxwell model, provides an outline to analyze the gas permeation properties of model systems with CMS and DEA in glassy polymer phase. The new model is developed by modifying the basic Maxwell MMMs model. The modification also includes the optimization of ldm, which is defined as the ratio of dispersed phase permeability to matrix permeability, and the determination of permeability of the dispersed phase. Furthermore, this Maxwell model has been extended to model the performance of amine mixed matrix membranes by incorporation of combined volume fraction of filler and amine 4* ad. The proposed approach can predict the permeability of CO2 through amine MMMs and also lowers the AARE value. This journal is © The Royal Society of Chemistry 2016. Royal Society of Chemistry 2016 Article PeerReviewed Nasir, R. and Mukhtar, H. and Man, Z. (2016) Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model. RSC Advances, 6 (36). pp. 30130-30138. https://www.scopus.com/inward/record.uri?eid=2-s2.0-84978602346&doi=10.1039%2fc5ra27756f&partnerID=40&md5=0d0cd0774ca866c357b8f82f95aed43e
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Institutional Repository
url_provider http://eprints.utp.edu.my/
description The incorporation of highly selective molecular sieve such as carbon molecular sieve (CMS) and highly affinitive solvent such as diethanolamine (DEA) into polyethersulfone (PES) have been implemented to synthesize amine mixed matrix membranes (MMMs) with an enhanced gas performance. Synergetic effect of CMS and DEA has caused the improvement of carbon dioxide (CO2) permeability and ideal CO2/CH4 selectivity. While existing theoretical models define the relative permeability well for binary mixed matrix membranes they fail to predict the relative permeability of amine mixed matrix membranes. In fact, the degree of deviation from the simple model predictions provides understanding into the detailed properties of the third component, which has been neglected in previous analyses of these models. Modification of an existing model, namely the Maxwell model, provides an outline to analyze the gas permeation properties of model systems with CMS and DEA in glassy polymer phase. The new model is developed by modifying the basic Maxwell MMMs model. The modification also includes the optimization of ldm, which is defined as the ratio of dispersed phase permeability to matrix permeability, and the determination of permeability of the dispersed phase. Furthermore, this Maxwell model has been extended to model the performance of amine mixed matrix membranes by incorporation of combined volume fraction of filler and amine 4* ad. The proposed approach can predict the permeability of CO2 through amine MMMs and also lowers the AARE value. This journal is © The Royal Society of Chemistry 2016.
format Article
author Nasir, R.
Mukhtar, H.
Man, Z.
spellingShingle Nasir, R.
Mukhtar, H.
Man, Z.
Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model
author_facet Nasir, R.
Mukhtar, H.
Man, Z.
author_sort Nasir, R.
title Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model
title_short Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model
title_full Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model
title_fullStr Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model
title_full_unstemmed Prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the Maxwell model
title_sort prediction of gas transport across amine mixed matrix membranes with ideal morphologies based on the maxwell model
publisher Royal Society of Chemistry
publishDate 2016
url http://scholars.utp.edu.my/id/eprint/22060/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84978602346&doi=10.1039%2fc5ra27756f&partnerID=40&md5=0d0cd0774ca866c357b8f82f95aed43e
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score 13.211869