Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior

Correlation equations for expressing the boiling temperature as direct function of liquid composition have been tested successfully and applied for predicting azeotropic behavior of multicomponent mixtures and the kind of azeotrope (minimum, maximum and saddle type) using modified correlation of Gib...

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Autor principal:	Khalid Farhod Chasib Al-Jiboury
Formato:	article
Lenguaje:	EN
Publicado:	Al-Khwarizmi College of Engineering – University of Baghdad 2007
Materias:	Vapor-Liquid Equilibria Azeotropic Behavior Multicomponent system Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040
Acceso en línea:	https://doaj.org/article/27507d1567934720909171403e0d40c4
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spelling	oai:doaj.org-article:27507d1567934720909171403e0d40c42021-12-02T03:50:19ZCorrelation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior1818-1171https://doaj.org/article/27507d1567934720909171403e0d40c42007-01-01T00:00:00Zhttp://www.iasj.net/iasj?func=fulltext&aId=2296https://doaj.org/toc/1818-1171Correlation equations for expressing the boiling temperature as direct function of liquid composition have been tested successfully and applied for predicting azeotropic behavior of multicomponent mixtures and the kind of azeotrope (minimum, maximum and saddle type) using modified correlation of Gibbs-Konovalov theorem. Also, the binary and ternary azeotropic point have been detected experimentally using graphical determination on the basis of experimental binary and ternary vapor-liquid equilibrium data.<br />In this study, isobaric vapor-liquid equilibrium for two ternary systems: 1-Propanol Hexane Benzene and its binaries 1-Propanol Hexane, Hexane Benzene and 1-Propanol Benzene and the other ternary system is Toluene Cyclohexane iso-Octane (2,2,4-Trimethyl-Pentane) and its binaries Toluene Cyclohexane, Cyclohexane iso-Octane and Toluene iso-Octane have been measured at 101.325 KPa. The measurements were made in recirculating equilibrium still with circulation of both the vapor and liquid phases. The ternary system 1-Propanol Hexane Benzene which contains polar compound (1-Propanol) and the two binary systems 1-Propanol Hexane and 1-Propanol Benzene form a minimum azeotrope, the other ternary system and the other binary systems do not form azeotrope.All the data passed successfully the test for thermodynamic consistency using McDermott-Ellis test method (McDermott and Ellis, 1965).The maximum likelihood principle is developed for the determination of correlations parameters from binary and ternary vapor-liquid experimental data which provides a mathematical and computational guarantee of global optimality in parameters estimation for the case where all the measured variables are subject to errors and the non ideality of both vapor and liquid phases for the experimental data for the ternary and binary systems have been accounted.The agreement between prediction and experimental data is good. The exact value should be determined experimentally by exploring the concentration region indicated by the computed valuesKhalid Farhod Chasib Al-JibouryAl-Khwarizmi College of Engineering – University of BaghdadarticleVapor-Liquid EquilibriaAzeotropic BehaviorMulticomponent systemChemical engineeringTP155-156Engineering (General). Civil engineering (General)TA1-2040ENAl-Khawarizmi Engineering Journal, Vol 3, Iss 2, Pp 67-86 (2007)
institution	DOAJ
collection	DOAJ
language	EN
topic	Vapor-Liquid Equilibria Azeotropic Behavior Multicomponent system Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040
spellingShingle	Vapor-Liquid Equilibria Azeotropic Behavior Multicomponent system Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040 Khalid Farhod Chasib Al-Jiboury Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior
description	Correlation equations for expressing the boiling temperature as direct function of liquid composition have been tested successfully and applied for predicting azeotropic behavior of multicomponent mixtures and the kind of azeotrope (minimum, maximum and saddle type) using modified correlation of Gibbs-Konovalov theorem. Also, the binary and ternary azeotropic point have been detected experimentally using graphical determination on the basis of experimental binary and ternary vapor-liquid equilibrium data.<br />In this study, isobaric vapor-liquid equilibrium for two ternary systems: 1-Propanol Hexane Benzene and its binaries 1-Propanol Hexane, Hexane Benzene and 1-Propanol Benzene and the other ternary system is Toluene Cyclohexane iso-Octane (2,2,4-Trimethyl-Pentane) and its binaries Toluene Cyclohexane, Cyclohexane iso-Octane and Toluene iso-Octane have been measured at 101.325 KPa. The measurements were made in recirculating equilibrium still with circulation of both the vapor and liquid phases. The ternary system 1-Propanol Hexane Benzene which contains polar compound (1-Propanol) and the two binary systems 1-Propanol Hexane and 1-Propanol Benzene form a minimum azeotrope, the other ternary system and the other binary systems do not form azeotrope.All the data passed successfully the test for thermodynamic consistency using McDermott-Ellis test method (McDermott and Ellis, 1965).The maximum likelihood principle is developed for the determination of correlations parameters from binary and ternary vapor-liquid experimental data which provides a mathematical and computational guarantee of global optimality in parameters estimation for the case where all the measured variables are subject to errors and the non ideality of both vapor and liquid phases for the experimental data for the ternary and binary systems have been accounted.The agreement between prediction and experimental data is good. The exact value should be determined experimentally by exploring the concentration region indicated by the computed values
format	article
author	Khalid Farhod Chasib Al-Jiboury
author_facet	Khalid Farhod Chasib Al-Jiboury
author_sort	Khalid Farhod Chasib Al-Jiboury
title	Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior
title_short	Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior
title_full	Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior
title_fullStr	Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior
title_full_unstemmed	Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior
title_sort	correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior
publisher	Al-Khwarizmi College of Engineering – University of Baghdad
publishDate	2007
url	https://doaj.org/article/27507d1567934720909171403e0d40c4
work_keys_str_mv	AT khalidfarhodchasibaljiboury correlationforfittingmulticomponentvaporliquidequilibriadataandpredictionofazeotropicbehavior
_version_	1718401595098529792

Correlation for fitting multicomponent vapor-liquid equilibria data and prediction of azeotropic behavior

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