Vapor-liquid equilibrium data and their correlation for binary systems consisting of ethanol, 2-propanol, 1,2-ethanediol and methyl benzoate

Fluid Phase Equilibria

Volumn 169, Issue 1, 2000, Pages 75-84

  Li, Jiding ^a   Chen, Cuixian ^a   Wang, Juan ^a  

^a TSINGHUA UNIVERSITY   (China)

Author keywords

Experimental data; Thermodynamic model; Vapor liquid equilibria

Indexed keywords

ATMOSPHERIC PRESSURE; BINARY MIXTURES; CORRELATION METHODS; ETHANOL; MATHEMATICAL MODELS; PRESSURE EFFECTS; PROPANE; THERMODYNAMICS;

ETHANEDIOL; METHYL BENZOATE; PROPANOL;

PHASE EQUILIBRIA;

2 PROPANOL; ALCOHOL; BENZOIC ACID DERIVATIVE; ETHYLENE GLYCOL; METHYL GROUP;

ARTICLE; ATMOSPHERIC PRESSURE; CHEMICAL COMPOSITION; CONTROLLED STUDY; EQUILIBRIUM CONSTANT; LIQUID; MATHEMATICAL MODEL; THERMODYNAMICS; VAPOR;

EID: 0034598873     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0378-3812(99)00340-4     Document Type: Article

References (19)

1. Berg L., Vosburgh M.G., Christensen R.W., Shanahan M.J. The separation of lower boiling alcohols by extractive distillation. Chem. Eng. Comm. 66:1988;1-21.
2. Gmehling J., Onken U., Arlt W., Grenzheuser P., Kolbe B., Rarey J.R., Weidlich U. Vapor-liquid equilibrium data collection. DECHEMA Chemistry Data Series. Vol. I:1977;DECHEMA, Frankfurt. 16 Parts.
3. Zielkiewicz J., Oracz P., Warycha S. Total vapor pressure measurements and excess Gibbs energies for the binary systems methanol+ethanol, ethanol+2-propanol, benzene+cyclohexane, benzene+carbon tetrachloride and benzene+ethanol at 303.15 and 313.15 K. Fluid Phase Equilib. 58:1990;191-209.
4. Kojima K. Activity coefficients at infinite dilution for ternary system. AIChE J. 18:1972;133-137.
5. Pradhan A.G., Bhethanabotla V.R., Campbell S.W. Vapor-liquid equilibrium data for ethanol-n-heptane-1-propanol and ethanol-n-heptane-2-propanol and their interpretation by a simple association model. Fluid Phase Equilib. 84:1993;183-206.
6. E for water/ethylene glycol/ethanol at 50°C. J. Chem. Eng. Data. 28:1983;410-412.
7. Liu F., Huang F., Zhang C.-H., Zhang C.-F. Mathematical modelling and identification in extractive distillation of alcohol-water with glycol and diethylene glycol. J. East China Institute of Chemical Technology. 19:1993;254-262. in Chinese.
8. Thorat R.T., Nageshwar G.D., Mene P.S. Indian Chem. Eng. 20:1978;37.
9. Li J.-D., Li Y.-G., Lu J.-F., Teng T. A new analytic formula for molecular radial distribution function in fluid and fluid mixtures. Fluid Phase Equilib. 55:1990;75-85.
10. Li Y.-G., Li J.-D., Lu J.-F., Teng T. A new model for metal solvent extraction system. Fluid Phase Equilib. 53:1989;235-242.
11. Zhou X., Ni L., Han S. J. Chem. Ind. Eng. 41:1990;122.
12. Yu Y.-X., Liu J.-G., Gao G.-H. Isobaric vapor-liquid equilibria of three aromatic hydrocarbon-tetraethylene glycol systems. Fluid Phase Equilib. 157:1999;299-307.
13. Abrams D.S., Prausnitz J.M. Statistical thermodynamics of liquid mixtures: a new expression for the excess Gibbs energy of partly or completely miscible systems. AIChE J. 21:1975;116-128.
14. Renon H., Prausnitz J.M. Local composition in thermodynamic excess functions for liquid mixtures. AIChE J. 14:1968;135-144.
15. Weast R.C. CRC Handbook of Chemistry and Physics. 66th edn. 1986;CRC Press, Florida.
16. Riddick J.A., Bunger W.B., Sakano T.K. Organic Solvents. 4th edn. 1986;Wiley, New York.
17. Herington E.F.G. J. Inst. Petrol. 37:1951;457.
18. AIChE, DIPPR Tables of Physical and Thermodynamic Properties of Pure Compounds, New York, 1984.
19. Nelder J.A., Mead R. A simplex method for function minimization. Comput. J. 7:1965;308-313.