Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid

碩士 === 國立臺灣科技大學 === 化學工程系 === 91 === A static-type apparatus with a liquid-phase circulation loop was used to measure isothermal vapor-liquid equilibrium ( VLE ) data for the binary systems of methyl benzoate + benzoic acid, ethyl benzoate + benzoic acid, and water + benzoic acid at temperatures fro...

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Main Author: 吳瞬膛
Other Authors: 林河木
Format: Others
Language:zh-TW
Published: 2003
Online Access:http://ndltd.ncl.edu.tw/handle/05470416646026879124
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spelling ndltd-TW-091NTUST3420292016-06-20T04:16:00Z http://ndltd.ncl.edu.tw/handle/05470416646026879124 Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid 苯甲酸混合物之汽液平衡量測 吳瞬膛 碩士 國立臺灣科技大學 化學工程系 91 A static-type apparatus with a liquid-phase circulation loop was used to measure isothermal vapor-liquid equilibrium ( VLE ) data for the binary systems of methyl benzoate + benzoic acid, ethyl benzoate + benzoic acid, and water + benzoic acid at temperatures from 413.15 K to 453.15 K. The experimental results exhibited no azeotrope formation. These VLE data are needed for design of separation process of azeotropic water/ethanol mixture with reactive distillation method. The binary VLE data were correlated satisfactorily with the NRTL and the UNIQUAC models, respectively. These VLE data were also used to test the two versions of UNIFAC model. The calculated results showed that the version of 1982 (UNIFAC-82) yielded better prediction for methyl benzoate + benzoic acid and ethyl benzoate + benzoic acid systems. 林河木 李明哲 2003 學位論文 ; thesis 74 zh-TW
collection NDLTD
language zh-TW
format Others
sources NDLTD
description 碩士 === 國立臺灣科技大學 === 化學工程系 === 91 === A static-type apparatus with a liquid-phase circulation loop was used to measure isothermal vapor-liquid equilibrium ( VLE ) data for the binary systems of methyl benzoate + benzoic acid, ethyl benzoate + benzoic acid, and water + benzoic acid at temperatures from 413.15 K to 453.15 K. The experimental results exhibited no azeotrope formation. These VLE data are needed for design of separation process of azeotropic water/ethanol mixture with reactive distillation method. The binary VLE data were correlated satisfactorily with the NRTL and the UNIQUAC models, respectively. These VLE data were also used to test the two versions of UNIFAC model. The calculated results showed that the version of 1982 (UNIFAC-82) yielded better prediction for methyl benzoate + benzoic acid and ethyl benzoate + benzoic acid systems.
author2 林河木
author_facet 林河木
吳瞬膛
author 吳瞬膛
spellingShingle 吳瞬膛
Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid
author_sort 吳瞬膛
title Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid
title_short Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid
title_full Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid
title_fullStr Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid
title_full_unstemmed Vapor-Liquid Equilibria for Mixtures Containing Benzoic Acid
title_sort vapor-liquid equilibria for mixtures containing benzoic acid
publishDate 2003
url http://ndltd.ncl.edu.tw/handle/05470416646026879124
work_keys_str_mv AT wúshùntáng vaporliquidequilibriaformixturescontainingbenzoicacid
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