Ternary Vapor-liquid Equilibrium for Benzene, Ethanol, and N-heptane PDF Download
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Author: Irven Frederick Wagner
Publisher:
ISBN:
Category :
Languages : en
Pages : 68
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Author: Irven Frederick Wagner
Publisher:
ISBN:
Category :
Languages : en
Pages : 68
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Author: Sheau Jean Fu
Publisher:
ISBN:
Category :
Languages : en
Pages : 0
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Binary and ternary vapor-liquid equilibrium data were determined at 75°C for the mixture of benzene, n-heptane and n-propyl alcohol using a modified Gillespie type of still. The equilibrium data for the three binary and the ternary systems are considered to be thermodynamically consistent as shown from the consistency test. Correlating the data with the Redlich-Kister equations for the binary and ternary systems shows that these equations would represent the data accurately over the entire range of compositions. The experimental results indicate that two binary systems, namely, n-heptane-n-propyl alcohol and n-propyl alcohol-benzene form an azeotrope at 75°C. Nevertheless no ternary azeotrope is found from the experiment.
Author: Sheau Jean Fu
Publisher:
ISBN:
Category : University of Ottawa theses
Languages : en
Pages : 262
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Author: Leon Robert Kiley
Publisher:
ISBN:
Category :
Languages : en
Pages : 534
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Author: James C. K. Ho
Publisher:
ISBN:
Category :
Languages : en
Pages : 0
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This thesis comprises of two parts. The first part is the determination of vapor-liquid equilibrium data at atmospheric pressure and 55°C for the ternary system n-hexane-ethyl alcohol-benzene and for the three possible binary systems n-hexane-ethyl alcohol, n-hexane-benzene and ethyl alcohol-benzene which constituted the ternary system. A modified Gillespie equilibrium still is employed to conduct the investigation. The equilibrium data for the three binary systems and the ternary system appear to be consistent as shown from the thermodynamic consistency tests. The experimental results indicate that two binary systems, namely, n-hexane-ethyl alcohol and ethyl alcohol-benzene form azeotrope at 760 nm. Hg. and 55°C. The ternary system deviates considerably from ideal liquid phase behavior. However, no ternary azeotrope is found from the experiment. The second part presents a method for predicting binary vapor-liquid equilibrium data at various conditions if the equilibrium data for the system concerned are available over the complete concentration range at any one isothermal or isobaric condition. The proposed method is limited to nonazeotropic solutions.
Author: Chii-Hwang Perng
Publisher:
ISBN:
Category :
Languages : en
Pages : 248
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Author: Hatim M. Eissa
Publisher: LAP Lambert Academic Publishing
ISBN: 9783847347118
Category :
Languages : en
Pages : 140
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Liquid-liquid equilibrium data of toluene or benzene+n-hexane or n-heptane or n-octane hydrocarbon systems are reported with many solvent mixtures at 298.15K.Complete phase digrams were obtained by evaluating the solubility and tie line results for each ternary mixture. The thermodynamic models: NRTL, UNIQUAC, and UIFAC models were used to correlate the experimental data and to predict the phase compositions of the ternary systems.The NRTL equation fitted the experimental data better than the UNIQUAC and UNIFAC equations: the average root mean square deviations (RMSD) was 0.165 for NRTL as compared to 0.491 for UNIQUAC and 1.304 for UNIFA
Author: James Lee Jones
Publisher:
ISBN:
Category : Alcohol
Languages : en
Pages : 82
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Author: Richard Alan Waldo
Publisher:
ISBN:
Category :
Languages : en
Pages : 98
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Author:
Publisher:
ISBN:
Category :
Languages : en
Pages : 22
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