Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic Membrane

The pervaporation using a commercial hydrophilic ceramic membrane supplied from PERVATECH was conducted. The dehydration of ethanol/ water system was used as a model for the pervaporation study. Pervaporation experiments of ethanol/water system were carried out in the temperature range of 303-343K,...

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Main Authors: Ameel Mohammed Rahman Al-Mayah, Zyad Rafaa Zair, Maha Hadi Al-Hassani
Format: Article
Language:English
Published: Al-Khwarizmi College of Engineering – University of Baghdad 2012-12-01
Series:Al-Khawarizmi Engineering Journal
Subjects:
Online Access:http://alkej.uobaghdad.edu.iq/index.php/alkej/article/view/152
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spelling doaj-fd59409dc6444106bd025fbd6e69a1542020-11-24T21:22:09Zeng Al-Khwarizmi College of Engineering – University of BaghdadAl-Khawarizmi Engineering Journal1818-11712312-07892012-12-0184Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic MembraneAmeel Mohammed Rahman Al-Mayah0Zyad Rafaa Zair1Maha Hadi Al-Hassani2Department of Biochemical Engineering /Al-Khwarizmi College of Engineering/University of BaghdadDepartment of Biochemical Engineering /Al-Khwarizmi College of Engineering/University of BaghdadDepartment of Chemical Engineering /College of Engineering/University of Baghdad The pervaporation using a commercial hydrophilic ceramic membrane supplied from PERVATECH was conducted. The dehydration of ethanol/ water system was used as a model for the pervaporation study. Pervaporation experiments of ethanol/water system were carried out in the temperature range of 303-343K, ethanol concentration in the feed 10-90 vol. % and the feed flow rate in the range of 0.5-10 L/min.  In this work, the effect of operation parameters on permeates fluxes as well as permeates separation factors have been studied. The Water flux is strongly dependent on the temperature; it increased with increasing in temperature, which in turn decreased the selectivity of membrane to water molecules. In addition water flux was decreased with increasing of ethanol concentration and increased with increasing feed flow rate. The optimal operational conditions of pervaporation process are: T=333 K, feed flow rate 6 L/min, and 90 vol.% ethanol concentration in the feed. High values of water flux and separation factor were obtained. The final results agreed well with other studies reported in the literature. http://alkej.uobaghdad.edu.iq/index.php/alkej/article/view/152Pervaporationethanol dehydrationbioethanolhydrophilic ceramic membranesilica
collection DOAJ
language English
format Article
sources DOAJ
author Ameel Mohammed Rahman Al-Mayah
Zyad Rafaa Zair
Maha Hadi Al-Hassani
spellingShingle Ameel Mohammed Rahman Al-Mayah
Zyad Rafaa Zair
Maha Hadi Al-Hassani
Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic Membrane
Al-Khawarizmi Engineering Journal
Pervaporation
ethanol dehydration
bioethanol
hydrophilic ceramic membrane
silica
author_facet Ameel Mohammed Rahman Al-Mayah
Zyad Rafaa Zair
Maha Hadi Al-Hassani
author_sort Ameel Mohammed Rahman Al-Mayah
title Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic Membrane
title_short Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic Membrane
title_full Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic Membrane
title_fullStr Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic Membrane
title_full_unstemmed Dehydration of Ethanol Using Pervaporation Separation with Nanoporous Hydrophilic Silica Ceramic Membrane
title_sort dehydration of ethanol using pervaporation separation with nanoporous hydrophilic silica ceramic membrane
publisher Al-Khwarizmi College of Engineering – University of Baghdad
series Al-Khawarizmi Engineering Journal
issn 1818-1171
2312-0789
publishDate 2012-12-01
description The pervaporation using a commercial hydrophilic ceramic membrane supplied from PERVATECH was conducted. The dehydration of ethanol/ water system was used as a model for the pervaporation study. Pervaporation experiments of ethanol/water system were carried out in the temperature range of 303-343K, ethanol concentration in the feed 10-90 vol. % and the feed flow rate in the range of 0.5-10 L/min.  In this work, the effect of operation parameters on permeates fluxes as well as permeates separation factors have been studied. The Water flux is strongly dependent on the temperature; it increased with increasing in temperature, which in turn decreased the selectivity of membrane to water molecules. In addition water flux was decreased with increasing of ethanol concentration and increased with increasing feed flow rate. The optimal operational conditions of pervaporation process are: T=333 K, feed flow rate 6 L/min, and 90 vol.% ethanol concentration in the feed. High values of water flux and separation factor were obtained. The final results agreed well with other studies reported in the literature.
topic Pervaporation
ethanol dehydration
bioethanol
hydrophilic ceramic membrane
silica
url http://alkej.uobaghdad.edu.iq/index.php/alkej/article/view/152
work_keys_str_mv AT ameelmohammedrahmanalmayah dehydrationofethanolusingpervaporationseparationwithnanoporoushydrophilicsilicaceramicmembrane
AT zyadrafaazair dehydrationofethanolusingpervaporationseparationwithnanoporoushydrophilicsilicaceramicmembrane
AT mahahadialhassani dehydrationofethanolusingpervaporationseparationwithnanoporoushydrophilicsilicaceramicmembrane
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