pρT measurements and EoS predictions of glycol ethers from (283.15 to 353.15) K at pressures up to 25 MPa

Journal of Chemical and Engineering Data

Volumn 49, Issue 5, 2004, Pages 1400-1405

  Lugo, Luis ^a   López, Enriqueta R ^a   Comuñas, María J P ^a   García, Josefa ^a,b   Fernàndez, Josefa ^a  

^a UNIVERSITY OF SANTIAGO DE COMPOSTELA   (Spain)

^b UNIVERSITY OF VIGO   (Spain)

Author keywords

[No Author keywords available]

Indexed keywords

ATMOSPHERIC PRESSURE; DATA REDUCTION; EQUATIONS OF STATE; ETHERS; LAWS AND LEGISLATION; PRESSURE EFFECTS; PROBABILITY DENSITY FUNCTION; THERMAL EXPANSION; VAPOR PRESSURE; VOLUMETRIC ANALYSIS;

DENSIMETERS; ISOTHERMAL COMPRESSIBILITY; LEE-KESLER METHOD; OIL ADDITIVES;

GLYCOLS;

EID: 4644327062     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je049893r     Document Type: Article

References (43)

1. Esteve, X.; Coneaa, A.; Coronas, A. Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene Glycol Dialkyl Ethers. J. Chem. Eng. Data 2003, 43, 392-397.
2. Ulrich, M. Genosorb for cleaning gas streams and recovery of useful materials. Hoechst Hig. Chem. Mag. 1992, 13, 26-30.
3. Liu, Y.-L.; Chiou, D.-R.; Chen, L.-J. Liquid-Liquid Equilibria for the Ternary System Water + Octane + Diethylene Glycol Monobutyl Ether. J. Chem. Eng. Data 2002, 47, 310-312.
4. j Binary Systems. J. Chem. Eng. Data 1999, 44, 261-253.
5. López, E. R.; Lugo, L.; Comuñas, M. J. P.; García, J.; Fernández, J. Liquid Density Measurements of Diethylene Glycol Monoalkyl Ethers as a Function of Temperature and Pressure. J. Chem. Eng. Data 2004, 49, 376-379.
6. Lugo, L.; Comuñas, M. J. P.; López, E. R.; Fernández, J. (p, Vm, T, x) measurements of Dimethyl Carbonate + Octane binary mixtures. I. Experimental results, isothermal compressibilities, isobaric expansivities and internal pressures. Fluid Phase Equilib. 2001, 186, 236-255.
7. Comuñas, M. J. P.; López, E. R.; Pires, P.; García, J.; Fernández, J. ppT measurements of poly(ethylene glycol) dimethyl ethers between 278.15 and 328.15 K at pressures to 12 MPa. Int. J. Thermophys. 2000, 21, 831-851.
8. Bouchot, C.; Richon, D. An enhanced method to calibrate vibrating tube densimeters. Fluid Phase Eguilibr. 2001, 191, 189-208.
9. Lagourette, B.; Boned, C.; Saint-Guirons, H.; Xans, P.; Zhou, H. Densimeter calibration method versus temperature and pressure. Meas. Sci. Technol. 1982, 3, 699-703.
10. Wagner, W.; Pruss, A. The IAPWS Formulation 1995 for the Thermodynamic Properties of Ordinary Water Substance for General and Scientific Use. J. Phys. Chem. Ref. Data 2002, 31, 387-535.
11. 16: A Critical Evaluation of Experimental Data. J. Chem. Eng. Data 1996, 41, 657-668.
12. Sokolowski, A.; Burczyk, B. Acetals and ethers. Part IV. Synthesis of acetals from aliphatic aldehydes and monoalkyl ethers of ethylene glycols. Pol. J. Chem. 1979, 53, 905-912.
13. Chiao, T.-T.; Thompson, A. R. Densities and Refractive Indexes of Diethylene Glycol Ether-Water Solutions: Diethylene Glycol Monomethyl, Monoethyl, and Monobutyl Ethers. J. Chem. Eng. Data 1961, 6, 192-193.
14. 8), 1-butanol, dibutyl ether, or 2,5-dioxahexane. Int. DATA Ser., Sel. Data Mixtures, Ser. A 1988, 2, 80-103.
15. Douheret, G.; Salgado, C.; Davis, M. I.; Loya, J. Ultrasonic speeds and isentropic functions of 2-(2-alkoxyethoxy)ethanol + water at 298.15 K. Thermochim. Acta 1992, 207, 313-328.
16. Pal, A.; Kumar, A. Excess molar volumes and viscosities of binary mixtures of 2-(2-butoxyethoxy)ethanol with chloroalkanes at 298.15 K. Fluid Phase Equilib. 1998, 143, 241-252.
17. Pal, A.; Sharma, S. Viscosities and Densities of Some n-Alkoxyethanols with Trichloroethylene and Tetrachloroethylene at 298.15 K. J. Chem. Eng. Data 1998, 43, 21-24.
18. Francesconi, R.; Castellari, C.; Comelli, F. Excess Molar Enthalpies and Excess Molar Volumes of Diethyl Carbonate + Some n-Alkoxyethanols at (298.15 and 313.15) K. J. Chem. Eng. Data 1999, 44, 1373-1378.
19. Pal, A.; Sharma, S.; Kumar, H. Excess molar volumes and viscosities of binary mixtures of some n-alkoxyethanols with propylamine at 298.15 K. Can. J. Chem. 2000, 78, 427-435.
20. Wiseman, P.; Heggie, M.; Palepu, R. Viscosities and thermodynamics of viscous flow of binary liquid mixtures of 2-(2-butoxyethoxy)ethanol with aniline and N-alkyl anilines. Can. J. Chem. 1992, 70, 2645-2649.
21. Ku, S.-C.; Peng, I.-H.; Tu, C.-H. Density and Viscosity of Mixtures of Alkoxypropanols with Ethanol at T = (298.15, 308.15, and 318.15) K. J. Chem. Eng. Data 2001, 46, 1392-1398.
22. Rowlinson, J. S.; Swinton, F. L., Liquids and Liquid Mixtures, 3rd ed.; Butterworth & Co.: London, 1982.
23. Comuñas, M. J. P.; Baylaucq, A.; Boned, C.; Fernández, J. Volumetric Properties of Monoethylene Glycol Dimethyl Ether and Diethylene Glycol Dimethyl Ether up to 60 MPa. J. Chem. Eng. Data 2003, 48, 1044-1049.
24. Comuñas, M. J. P.; Baylaucq, A.; Boned, C.; Fernández, J. High-Pressure Measurements of the Viscosity and Density of Two Polyethers and Two Dialkyl Carbonates. Int. J. Thermophys. 2001, 22, 749-768.
25. Valderrama, J. O. The State of the Cubic Equations of State. Ind. Eng. Chem. Res. 2003, 42, 1603-1618.
26. Wei, Y. S.; Sadus, R. J. Equations of state for the calculation of fluid-phase equilibria. AIChE J. 2000, 46, 169-196.
27. Lugo, L.; García, J.; Comuñas, M. J. P.; Fernández, J. Phase Equilibria and PVT predictions for alkyl carbonate + n-alkane systems using equations of state. Fluid Phase Equilib. 2003, 212, 111-128.
28. Baylaucq, A.; Comuñas, M. J. P.; Fernández, J.; Boned, C.; Allal, A. High-pressure viscosity and density modeling of two polyethers and two dialkyl carbonates. Fluid Phase Equilib. 2002, 199, 249-263.
29. Soave, G. Equilibrium constants from a modified Redlich-Kwong equation of state. Chem. Eng. Sci. 1972, 27, 1197-1203.
30. Peng, D. Y.; Robinson, D. B. A new two-constant equation of state. Ind. Chem. Eng. Fundam. 1976, 15, 59-64.
31. Peneloux, A.; Rauzy, E.; Freze, R. A consistent correction for Redlich-Kwong-Soave volumes. Fluid Phase Equilib. 1982, 5, 7-23.
32. Patel, N. C.; Teja, A. S. A new cubic equation of state for fluids and fluid mixtures. Chem. Eng. Sci. 1982, 37, 463-473.
33. Schmidt, G.; Wenzel, H. A modified van der Waals type equation of state. Chem. Eng. Sci. 1980, 35, 1503-1512.
34. Wilson, L. C.; Wilson, H. L.; Wilding, W. V.; Wilson, G. M. Critical Point Measurements for Fourteen Compounds by a Static Method and a Flow Method. J. Chem. Eng. Data 1996, 41, 1252-1254.
35. Teja, A. S.; Rosenthal, D. J. The critical pressures and temperatures of 10 substances using a low residence time flow apparatus. Experimental Results for Phase Equilibria and Pure Component Properties; DIPPR DATA Series No. 1, 1991.
36. Yan, X.; Dong, Q.; Hong, X. Reliability Analysis of Group-Contribution Methods in Predicting Critical Temperatures of Organic Compounds. J. Chem. Eng. Data 2003, 48, 374-380.
37. VonNierderhausern, D. M.; Wilson, L. C.; Giles, N. F.; Wilson, G. M. Critical-Point Measuraments for Nine Compounds by a Flow Method. J. Chem. Eng. Data 2000, 45, 154-156.
38. Dykyj, J.; Seprakova, M.; Maulech, J. Physikalische Eigenschaften des Athylenglykols und Seiner Derivate (II) Dampftensionen von Alkoxyathanolen und Aneren Drivaten des Athylenglykols. Chem. Zvesti 1957, 11, 461-466.
39. Stull, D. R. Vapor Pressure of Pure Substances Organic Compounds. Ind. Eng. Chem. 1947, 39, 517-540.
40. Gardner, G. S.; Brewer, J. E. Vapor Pressure of Commercial High-Boiling Organic Solvents. Ind. Eng. Chem. 1937, 29, 179-181.
41. Reid, R. C.; Prausnitz, J. M.; Poling, B. E. The Properties of Gases and Liquids; McGraw-Hill: New York, 1987.
42. Thermodynamics Source Database. In NIST Chemistry WebBook, NIST Standard Reference Database Number 69; Linstrom, P. J., Mallard, W. G., Eds.; National Institute of Standards and Technology: Gaithersburg, MD, March 2003 (http://webbook.nist.gov).
43. Akhundov, T. S.; Imanov, S. Y.; Tairov, A. D.; Sharipov, K. Observation of P-v-T dependence for diethylene glycol monoethyl ether. Izv. Vyssh. Uchebn. Zaved., Neft Gaz 1977, 20, 50-52 (in Russian).