New apparatus for the fast determination of high-pressure vapor-liquid equilibria of mixtures and of accurate critical pressures

Journal of Chemical and Engineering Data

Volumn 45, Issue 2, 2000, Pages 265-271

  Galicia Luna, Luis A ^a   Ortega Rodriguez, A ^a   Richon, D ^b  

^a INSTITUTO POLITÉCNICO NACIONAL   (Mexico)

^b PSL RESEARCH UNIVERSITY   (France)

Author keywords

[No Author keywords available]

Indexed keywords

ALCOHOLS; BUTANE; CARBON DIOXIDE; COMPOSITION; CURVE FITTING; ETHANOL; HIGH PRESSURE EFFECTS; HIGH TEMPERATURE OPERATIONS; MIXTURES; PHASE EQUILIBRIA; PRESSURE MEASUREMENT; VAPOR PRESSURE;

CRITICAL PRESSURE; HIGH PRESSURE EQUIPMENT; PROPANOL;

PRESSURE GAGES;

EID: 0033626947     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je990187d     Document Type: Article

References (21)

1. Baker, L. C. W.; Anderson, T. F. J. Am. Chem. Soc. 1957, 79, 2071.
2. Brunner, G. Industrial Process Development: Countercurrent Multistage Gas Extraction Processes. Proceedings of the 4th International Symposium on Supercritical Fluids, Sendai, Japan, May 11-14, 1997; Vol. C, pp 745-756.
3. Galicia-Luna, L. A.; Escobedo-Alvarado, G. N.; Díaz-Ramirez, N.; A New Mixing Rule for the Patel-Teja Equation of State. Will send to Ind. Eng. Chem. Res. 1999.
4. Gurdial, G. S.; Foster, N. R.; Yun, S. L. J.;Tilly, K. D. Phase behavior of supercritical fluid-entrainer systems. Supercritical Fluid Engineering Science; ACM Symposium Series No. 514; American Chemical Society: Washington, DC, 1993; pp 34-45.
5. IMSL. The IMSL Library; IMSL Inc.: Houston, 1979; Vol. 2.
6. Knapp, H.; Döring, R.; Oellrich, L.; Plöcker, U.; Prausnitz, J. M. Vapor-Liquid Equilibria, for Mixtures of Low boiling Substances; DECHEMA Chemistry Data Series Vol. VI; Frankfurt, 1982.
7. Laugier, S.; Richon, D. New apparatus to perfom fast determinations of mixtures vapor-liquid equilibria up to 10 MPa and 423 K. Rev. Sci. Instrum. 1986, 57, 469-472.
8. Lim, J. S.; Lee, Y. Y.; Chun, H. S. Phase Equilibria for Carbon Dioxide-Ethanol-Water System at Elevated Pressures. J. Supercrit. Fluids 1994, 7, 219-230.
9. 2+Etanol a 353.04 K y hasta 10.7 MPa. Proceedings of the International Symposium of the ESIQIE, May 27-29, 1998.
10. 2+n-Heptano a 353.04 K y hasta 11.6 MPa. Proceedings of the International Symposium of the ESIQIE, May 27-29, 1998.
11. Patel, N. C.; Teja, A. S. A New Cubic Equation of State for Fluids and Fluid Mixtures. Chem. Eng. Sci. 1982, 37, 463.
12. Peng, D. Y.; Robinson, D. B. A New Two-Constant Equation of State. Ind. Eng. Chem. Fundam. 1976, 15, 59.
13. Radosz, M. Vapor-liquid equilibrium for 2-propanol and carbon dioxide. J. Chem. Eng. Data 1986, 31, 43-45.
14. Reid, R. C.; Prausnitz, J. M.; Poling, B. E. The Properties of Gases & Liquids. McGraw-Hill: Singapore, 1986.
15. Renon, H.; Prausnitz, J.-M. Local composition in thermodynamic excess function for liquid mixtures. AIChE J. 1968, 14, 135-144.
16. Soave, G. Equilibrium Constants from a Modified Redlich-Kwong Equation of State. Chem. Eng. Sci. 1972, 1197.
17. Suzuki, K.; Sue, H.; Itou, M.; Smith, R. L.; Inomata, H.; Arai, K.; Saito, S. Isothermal vapor-liquid equilibrium data for binary systems high pressure: carbon dioxide-methanol, carbon dioxide-ethanol, carbon dioxide-1-propanol, methane-ethanol, methane-1-propanol, ethane-ethanol and ethane-1-propanol systems. J. Chem. Eng. Data 1990, 35, 63-66.
18. Takishima, S.; Saiki, K.; Arai, K.; Saito, S. J. J. Chem. Eng. Jpn. 1986, 19, 48.
19. Waxman, M.; Gallagher, J. S. Thermodynamic properties of isobutane for temperatures from 250 to 600 K and pressures from 0.1 to 40 MPa. J. Chem. Eng. Data 1983, 28, 224-241.
20. Wong, D. S. H.; Sandler, S. I. A Theoretically Correct Mixing Rule for Cubic Equations of State. AIChE J. 1992, 38, 671.
21. Yoon, J.-H.; Lee, H.-S.; Lee, H. High-Pressure Vapor-Liquid Equilibria for Carbon Dioxide + Methanol, Carbon Dioxide + Ethanol, and Carbon Dioxide + Methanol + Ethanol J. Chem. Eng. Data 1993, 38, 53-55.