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Pervaporation is a membrane separation process where the separation is based on the different affinity of the components to the membrane. Pervaporation is effective for separating azeotrope mixture since the separation not based on liquid-vapor equilibrium. In the pervaporation of ethanol-water, the...

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Main Author: (NIM 13003033), SUGIANTO
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/11450
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:11450
spelling id-itb.:114502017-09-27T11:39:34Z#TITLE_ALTERNATIVE# (NIM 13003033), SUGIANTO Indonesia Final Project INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/11450 Pervaporation is a membrane separation process where the separation is based on the different affinity of the components to the membrane. Pervaporation is effective for separating azeotrope mixture since the separation not based on liquid-vapor equilibrium. In the pervaporation of ethanol-water, the membrane used has to be hydrophilic and selective. Nowadays, zeolite membrane is widely used for dehydration ethanol with pervaporation since it has good hydrophilicity and stability.<p> <br /> <br /> <br /> The purpose of this study is to get zeolite NaA membrane that suitable for ethanol-water pervaporation. Beside that, the pervaporation performance of zeolite membrane NaA was intensively investigated. Zeolite membrane was prepared by hydrotermal synthesis from a gel as zeolit raw material placed in contact with the support surface and then heated. The variation of this study are gel concentration, synthesis methode, and operation condition of pervapoation like feed flow rate at 300, 1000, and 1500 cm3/minute and temperature at 25, 40, dan 60 degrees C.<p> <br /> <br /> <br /> In this study, the zeolite NaA membrane was prepared by hydrothermal synthesis that can be used for ethanol pervaporation. However the pervaporation performance and the membrane is far from satisfaction. The flux and selectivity were affected by both feed flow rate and operating temperature. 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 Pervaporation is a membrane separation process where the separation is based on the different affinity of the components to the membrane. Pervaporation is effective for separating azeotrope mixture since the separation not based on liquid-vapor equilibrium. In the pervaporation of ethanol-water, the membrane used has to be hydrophilic and selective. Nowadays, zeolite membrane is widely used for dehydration ethanol with pervaporation since it has good hydrophilicity and stability.<p> <br /> <br /> <br /> The purpose of this study is to get zeolite NaA membrane that suitable for ethanol-water pervaporation. Beside that, the pervaporation performance of zeolite membrane NaA was intensively investigated. Zeolite membrane was prepared by hydrotermal synthesis from a gel as zeolit raw material placed in contact with the support surface and then heated. The variation of this study are gel concentration, synthesis methode, and operation condition of pervapoation like feed flow rate at 300, 1000, and 1500 cm3/minute and temperature at 25, 40, dan 60 degrees C.<p> <br /> <br /> <br /> In this study, the zeolite NaA membrane was prepared by hydrothermal synthesis that can be used for ethanol pervaporation. However the pervaporation performance and the membrane is far from satisfaction. The flux and selectivity were affected by both feed flow rate and operating temperature.
format Final Project
author (NIM 13003033), SUGIANTO
spellingShingle (NIM 13003033), SUGIANTO
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author_facet (NIM 13003033), SUGIANTO
author_sort (NIM 13003033), SUGIANTO
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/11450
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