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Nowadays, needs of high purities alcohols in industry increase rapidly. Pervaporation is an alternative separation process using membrane which allows separation of alcohol-water mixtures at their azeotropic composition with low energy consumption. Separations can be obtained by using the difference...

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Main Author: GUSMELLI (NIM 13004106), INDRIA
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/8234
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:8234
spelling id-itb.:82342017-09-27T11:39:33Z#TITLE_ALTERNATIVE# GUSMELLI (NIM 13004106), INDRIA Indonesia Final Project INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/8234 Nowadays, needs of high purities alcohols in industry increase rapidly. Pervaporation is an alternative separation process using membrane which allows separation of alcohol-water mixtures at their azeotropic composition with low energy consumption. Separations can be obtained by using the difference of solubility and diffusivity of components. Pervaporation process performance is determined by flux and selectivity.<p> <br /> <br /> <br /> Hydrophilic membrane was used for dehydrating alcohols trough pervaporation. Previous research showed that using CA/Zeolite membrane could increase the pervaporation performance for ethanol-water separation. This research will study performance of CA/Zeolite membrane in separating alcohol-water mixtures and observe the effect of temperature toward pervaporation performance.<p> <br /> <br /> <br /> The research consists of membrane preparation, membrane characterization, and pervaporation. Feeds are ethanol-water, isopropanol-water, and 2-butanol-water mixtures at their azeotropic composition. Ethanol-water mixtures' composition are varying at 85%-v, azeotropic, dan 98%-v. Feeds temperature are varying between 40-60°C and downstren pressure 200 mbar. Polymeric membrane cellulose acetate (CA) will be used and modification will be done by depositing 20%-wt CA of zeolite Malang in the polymeric matrix. Research found that by depositing zeolite, flux increases for about 1,35-1,4 times and selectivity increases for about 3,5-8,2 times. 2butanol-air has the largest selectivity, followed by isopropanol and ethanol. text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description Nowadays, needs of high purities alcohols in industry increase rapidly. Pervaporation is an alternative separation process using membrane which allows separation of alcohol-water mixtures at their azeotropic composition with low energy consumption. Separations can be obtained by using the difference of solubility and diffusivity of components. Pervaporation process performance is determined by flux and selectivity.<p> <br /> <br /> <br /> Hydrophilic membrane was used for dehydrating alcohols trough pervaporation. Previous research showed that using CA/Zeolite membrane could increase the pervaporation performance for ethanol-water separation. This research will study performance of CA/Zeolite membrane in separating alcohol-water mixtures and observe the effect of temperature toward pervaporation performance.<p> <br /> <br /> <br /> The research consists of membrane preparation, membrane characterization, and pervaporation. Feeds are ethanol-water, isopropanol-water, and 2-butanol-water mixtures at their azeotropic composition. Ethanol-water mixtures' composition are varying at 85%-v, azeotropic, dan 98%-v. Feeds temperature are varying between 40-60°C and downstren pressure 200 mbar. Polymeric membrane cellulose acetate (CA) will be used and modification will be done by depositing 20%-wt CA of zeolite Malang in the polymeric matrix. Research found that by depositing zeolite, flux increases for about 1,35-1,4 times and selectivity increases for about 3,5-8,2 times. 2butanol-air has the largest selectivity, followed by isopropanol and ethanol.
format Final Project
author GUSMELLI (NIM 13004106), INDRIA
spellingShingle GUSMELLI (NIM 13004106), INDRIA
#TITLE_ALTERNATIVE#
author_facet GUSMELLI (NIM 13004106), INDRIA
author_sort GUSMELLI (NIM 13004106), INDRIA
title #TITLE_ALTERNATIVE#
title_short #TITLE_ALTERNATIVE#
title_full #TITLE_ALTERNATIVE#
title_fullStr #TITLE_ALTERNATIVE#
title_full_unstemmed #TITLE_ALTERNATIVE#
title_sort #title_alternative#
url https://digilib.itb.ac.id/gdl/view/8234
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