Pressure-density-temperature behavior of CO2/acetone, CO 2/ toluene, and CO2/monochlorobenzene mixtures in the near-critical region

Journal of Chemical and Engineering Data

Volumn 49, Issue 4, 2004, Pages 976-979

  Wu, Jialong ^a   Pan, Qinmin ^a   Rempel, Garry L ^a  

^a UNIVERSITY OF WATERLOO   (Canada)

Author keywords

[No Author keywords available]

Indexed keywords

ACETONE; BENZENE; CARBON DIOXIDE; CORRELATION METHODS; DENSITY (SPECIFIC GRAVITY); MIXTURES; PRESSURE; SOLVENTS; TEMPERATURE; TOLUENE;

AROMATICITY; CHEMICAL INERTNESS; CHIRALITY; CRITICAL REGION; MONOCHLOROBENZENE;

SUPERCRITICAL FLUIDS;

EID: 3342983297     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je0342771     Document Type: Article

References (23)

1. Eckert, C. A.; Knutson, B. L.; Debenedetti, P. G. Supercritical Fluids as Solvents for Chemical and Materials Processing. Nature 1996, 353, 313-318.
2. Phelps, C. L.; Smart, N. G.; Wai, C. M. Past, Present, and Possible Future Applications of Supercritical Fluid Extraction Technology, J. Chem. Educ. 1998, 73, 1163-1168.
3. Kiran, E.; Brennecke, J. F. Supercritical Fluid Engineering Science; American Chemical Society: Washington, DC, 1993.
4. Clifford T. Fundamentals of Supercritical Fluids; Oxford University Press: New York, 1999.
5. Chang, Chiehming J.; Day, Chany-Yih; Ko, Ching-Ming; Chiu, Kou-Lung. Densities and P-x-y Diagrams for Carbon Dioxide Dissolution in Methanol, Ethanol, and Acetone Mixtures. Fluid Phase Equilib. 1997, 131, 243-258.
6. 2 at Elevated Pressures. J. Chem. Eng. Data 1996, 41, 839-843.
7. Giacobbe, F. W. Thermodynamic Solubility Behavior of Carbon Dioxide in Acetone. Fluid Phase Equilib. 1992, 72, 277-297.
8. Katayama, T.; Ohgaki, K.; Maekawa, G.; Goto, M.; Nagano, T. Isothermal Vapor-Liquid Equilibria of Acetone-Carbon Dioxide and Methanol-Carbon Dioxide Systems at High Pressures. J. Chem. Eng. Jpn. 1975, 8, 89-92.
9. Sebastian, H. M.; Simnick, J. J.; Lin, H. M.; Chao, K. C. Gas-Liquid Equilibrium in Mixtures of Carbon Dioxide Plus Toluene and Carbon Dioxide Plus m-Xylene. J Chem. Eng. Data 1980, 25, 246-248.
10. Ng, Heng-Joo; Robinson, D. B. Equilibrium Phase Properties of the Toluene-Carbon Dioxide System. J. Chem. Eng. Data 1978, 23, 325-327.
11. Kim, Choon-Ho; Vimalchand, P.; Donohue, M. D. Vapor-Liquid Equilibria for Binary Mixtures of Carbon Dioxide with Benzene, Toluene and p-Xylene. Fluid Phase Equilib. 1980, 31, 299-311.
12. Toohigi, K.; Hasegawa, K.; Asano, N.; Kojima, K. Vapor-Liquid Equilibria for the Carbon Dioxide+Pentane and Carbon Dioxide+-Toluene Systems. J. Chem. Eng. Data 1998, 43, 954-956.
13. Reaves, J. T.; Griffith, A. T.; Roberts, C. B. Critical Properties of Dilute Carbon Dioxide+Entrainer and Ethane+Entrainer Mixtures. J. Chem. Eng. Data 1998, 43, 683-686.
14. Walther D.; Maurer G. High-Pressure Vapour-Liquid Equilibria in Binary Mixtures of Carbon Dioxide and Benzaldehyde, Bromobenzene, Chlorobenzene, 1,2-Dichlorobenzene and 2-Chloro-1-methylbenzene at Temperatures between 313 and 393 K and Pressures up to 22 MPa. Ber. Bunsen - Ges. Phys. Chem. 1992, 96, 981-988.
15. Guigard, S. E.; Stiver, W. H. A Density-Dependent Solute Solubility Parameter for Correlating Solubilities in Supercritical Fluids. Ind. Eng. Chem. Res. 1998, 37, 3786-3792.
16. Li, G. Exploratory Study on Hydrogenation of Acrylonitrile Butadiene Copolymer in Supercritical Carbon Dioxide. M.A.Sc. Thesis, University of Waterloo, Ontario, Canada, 2000.
17. Magee, J. W. Isochoric p-ρ-T measurements on Difluoromethane-(R32) from 142 to 396 K and Pentafluoroethane (R125) from 178 to 398 K at Pressures to 35 MPa. Int. J. Thermophys. 1996, 17, 803-822.
18. Huang, F.; Li, M.; Lee, L. L.; Starling, K. E.; Chung, F. T. H. Accurate Equation of State for Carbon Dioxide. J. Chem. Eng. Jpn. 1985, 18, 490-496.
19. Lacomb, R. H.; Sanchez, I. C. Statistical Thermodynamics of Fluid Mixtures. J. Phys. Chem. 1978, 80, 2563-2580.
20. Sanchez, I. C.; Lacomb, R. H. Statistical Thermodynamics of Polymer Solutions. Macromolecules. 1978, 11, 1145-1156.
21. Peng D.; Robinson D. B. A New Two-Constant Equation of State. Ind. Eng. Chem., Fundam. 1976, 15, 59-64.
22. Xiong, Y.; Kiran, E. Prediction of High-Pressure Phase Behaviour in Polyethylene/n-pentane/Carbon Dioxide Ternary System with the Sanchez-Lacombe Model. Polymer. 1994, 35, 4408-4415.
23. 2/Polystyrene Ternary System. J. Appl. Polym. Sci. 2002, 85, 1938-1944.