Isothermal vapour-liquid equilibria in the ternary system tert-butyl methyl ether + tert-butanol + 2,2,4-trimethylpentane and the three binary subsystems

Fluid Phase Equilibria

Volumn 180, Issue 1-2, 2001, Pages 235-245

  Bernatová, Svatoslava ^a   Wichterle, Ivan ^a  

^a INSTITUTE OF CHEMICAL PROCESS FUNDAMENTALS   (Czech Republic)

Author keywords

Experimental data; Molar excess volume; Prediction; Ternary mixture; Vapour liquid equilibrium

Indexed keywords

ORGANIC COMPOUNDS; TERNARY SYSTEMS;

BINARY SYSTEMS;

PHASE EQUILIBRIA;

2,2,4 TRIMETHYLPENTANE; TERT BUTYL ALCOHOL; TERT BUTYL METHYL ETHER; UNCLASSIFIED DRUG;

ARTICLE; BINARY MIXTURE; CONTROLLED STUDY; EXPERIMENT; ISOTHERM; LIQUID; MEASUREMENT; MIXTURE; MOLAR EXCESS VOLUME; PHASE EQUILIBRIUM; PHYSICAL PARAMETERS; PHYSICAL PHASE; PREDICTION; PRESSURE; TEMPERATURE; TERNARY MIXTURE; THERMODYNAMICS; VAPOR; VOLUME;

EID: 0035870532     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0378-3812(01)00349-1     Document Type: Article

References (12)

1. Wichterle I. Isothermal vapor-liquid equilibria in the ternary system propan-2-ol + diisopropyl ether + 2,2,4-trimethylpentane. ELDATA: Int. Electron. J. Phys. Chem. Data. 5:1995;179-189.
2. Teodorescu M., Aim K., Wichterle I. Isothermal vapour-liquid equilibria for pentan-3-one + 1,4-dichlorobutane, + trichloromethane, + 1,1,1-trichloroethane, + 1,1,2,2-tetrachloroethane binary systems. Fluid Phase Equilbr. 147:1998;215-228.
3. Linek J. Excess volumes of 1,1,2,2-tetrachloroethane + some n-alkyl n-alkanoates. ELDATA: Int. Electron. J. Phys. Chem. Data. 1:1995;23-28.
4. Hayden J.G., O'Connell J.P. Generalized method for predicting second virial coefficients. Ind. Eng. Chem., Proc. Des. Dev. 14:1975;209-216.
5. O.A. Hougen, K.M. Watson, Chemical Process Principles, Part II, Wiley, New York, 1947.
6. E. Hála, K. Aim, T. Boublík, J. Linek, I. Wichterle, Vapor-Liquid Equilibrium at Normal and Reduced Pressures (in Czech), Academia, Praha, 1982.
7. J. Gmehling, J. Menke, K. Fischer, J. Krafczyk, Azeotropic Data, Vols. 1-2, VCH Verlag, Weinheim, Germany, 1994, pp. 1-1729.
8. Martinez-Soria V., Pilar Pena M., Monton J.B. Vapor-liquid Equilibria for the binary systems tert-butyl alcohol + toluene, + isooctane, and + methylcyclohexane at 101.3 kPa. J. Chem. Eng. Data. 44:1999;148-151.
9. Valero J., Gracia M., Gutierrez Losa C. Thermodynamic study of association in t-butyl alcohol according to a two-constant model. J. Chim. Phys. Phys. Chim. Biol. 77:1980;65-68.
10. I. Wichterle, J. Linek, Z. Wagner, H.V. Kehiaian, Vapor-Liquid Equilibrium in Mixtures and Solutions, Bibliographic Database EVLM 2000, CD-ROM [ISBN 2-9507664-2-0], ELDATA Paris, France, 2000.
11. Fuangfoo S., Kesting M., Viswanath D.S. Isothermal vapor-liquid equilibria for methyl-2,2-dimethylethyl ether + 2-methylpropan-2-ol, diethyl ether + ethyl-2,2-dimethylethyl ether, 2-methyl-2-butene + (2-methylbutan-2-ol), and diisopropyl ether + octane. J. Chem. Eng. Data. 44:1999;405-410.
12. T. Boublík, K. Aim, The Vapour Pressures of Pure Substances, Elsevier, Amsterdam, in preparation.