Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water

The purpose of this investigation was to determine the effect of a homologous series of solutes on the overall mass-transfer coefficients for liquid-liquid extraction. The solutes used were ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, triethylene glycol dimethyl ether, and tetra...

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Main Author: Pusey, Robert H.
Other Authors: Chemical Engineering
Format: Others
Language:en_US
Published: Virginia Polytechnic Institute 2017
Subjects:
Online Access:http://hdl.handle.net/10919/76285
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spelling ndltd-VTETD-oai-vtechworks.lib.vt.edu-10919-762852020-09-29T05:43:29Z Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water Pusey, Robert H. Chemical Engineering LD5655.V855 1958.P874 Extraction (Chemistry) Mass transfer The purpose of this investigation was to determine the effect of a homologous series of solutes on the overall mass-transfer coefficients for liquid-liquid extraction. The solutes used were ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, triethylene glycol dimethyl ether, and tetraethylene glycol dimethyl ether. The carrier solvent was water, and the extracting solvent was toluene. The phase diagrams for these systems were determined at 30 °C. The phase diagrams were found to be similar and to have maximum solubilities ranging from 69.9 to 76.7 weight per cent of solute.. Three of the systems exhibited solutropes, and the system containing tetraethylene glycol dimethyl ether approached a solutrope at a solute concentration of approximately 64 per cent. A countercurrent-flow, 1-1/2-inch diameter, horizontal, pyrex glass tube, eight feet long with an interfacial surface area of one square foot, was used for the extraction tests. The feed concentration ranged from 9.10 to 15.18 weight per cent of solute in water. The flow rates of the water phase varied from 15.20 to 34.72 pounds per hour, and the solvent phase flow rates varied from 18.86 to 33.83 pounds per hour. The overall mass-transfer coefficients based on the water phase were found to vary between 0.0098 and 0.0133, 0.0036 and 0.0051, 0.0035 and 0.0063, and 0.0023 and 0.0063, for the systems investigated. The solvent phase coefficients were found to vary between 0.0097 and 0.0149, 0.0057 and 0.0079, 0.0092 and 0.0172, and 0.0087 and 0.0237. The overall coefficients were not affected appreciably by changing the molecular weight of the solute. Also, experimentally determined values of the overall coefficients based on the solvent phase did not agree with those values of the coefficients calculated by previously determined equations. Master of Science 2017-03-10T20:47:57Z 2017-03-10T20:47:57Z 1958 Thesis Text http://hdl.handle.net/10919/76285 en_US OCLC# 7566974 In Copyright http://rightsstatements.org/vocab/InC/1.0/ viii, 92, [3] leaves application/pdf application/pdf Virginia Polytechnic Institute
collection NDLTD
language en_US
format Others
sources NDLTD
topic LD5655.V855 1958.P874
Extraction (Chemistry)
Mass transfer
spellingShingle LD5655.V855 1958.P874
Extraction (Chemistry)
Mass transfer
Pusey, Robert H.
Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water
description The purpose of this investigation was to determine the effect of a homologous series of solutes on the overall mass-transfer coefficients for liquid-liquid extraction. The solutes used were ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, triethylene glycol dimethyl ether, and tetraethylene glycol dimethyl ether. The carrier solvent was water, and the extracting solvent was toluene. The phase diagrams for these systems were determined at 30 °C. The phase diagrams were found to be similar and to have maximum solubilities ranging from 69.9 to 76.7 weight per cent of solute.. Three of the systems exhibited solutropes, and the system containing tetraethylene glycol dimethyl ether approached a solutrope at a solute concentration of approximately 64 per cent. A countercurrent-flow, 1-1/2-inch diameter, horizontal, pyrex glass tube, eight feet long with an interfacial surface area of one square foot, was used for the extraction tests. The feed concentration ranged from 9.10 to 15.18 weight per cent of solute in water. The flow rates of the water phase varied from 15.20 to 34.72 pounds per hour, and the solvent phase flow rates varied from 18.86 to 33.83 pounds per hour. The overall mass-transfer coefficients based on the water phase were found to vary between 0.0098 and 0.0133, 0.0036 and 0.0051, 0.0035 and 0.0063, and 0.0023 and 0.0063, for the systems investigated. The solvent phase coefficients were found to vary between 0.0097 and 0.0149, 0.0057 and 0.0079, 0.0092 and 0.0172, and 0.0087 and 0.0237. The overall coefficients were not affected appreciably by changing the molecular weight of the solute. Also, experimentally determined values of the overall coefficients based on the solvent phase did not agree with those values of the coefficients calculated by previously determined equations. === Master of Science
author2 Chemical Engineering
author_facet Chemical Engineering
Pusey, Robert H.
author Pusey, Robert H.
author_sort Pusey, Robert H.
title Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water
title_short Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water
title_full Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water
title_fullStr Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water
title_full_unstemmed Overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water
title_sort overall mass-transfer coefficients for a homologous series of poly glycol ethers between toluene and water
publisher Virginia Polytechnic Institute
publishDate 2017
url http://hdl.handle.net/10919/76285
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