Phase behavior, densities, and isothermal compressibility of the CO 2 + pentane + acetone ternary system in various phase regions

Journal of Chemical and Engineering Data

Volumn 49, Issue 3, 2004, Pages 537-543

  Chen, Jiawei ^a   Wu, Weize ^a   Liu, Zhimin ^a   Jiang, Tao ^a   He, Jun ^a   Huang, Ying ^a   Yang, Guanying ^a   Han, Buxing ^a  

^a INSTITUTE OF CHEMISTRY   (China)

Author keywords

[No Author keywords available]

Indexed keywords

COMPRESSIBILITY OF LIQUIDS; EXTRACTION; ISOTHERMS; PHASE SEPARATION; PRESSURE EFFECTS; SUPERCRITICAL FLUIDS; TERNARY SYSTEMS; THERMAL EFFECTS;

ISOTHERMAL COMPRESSIBILITY; PHASE BEHAVIOR;

ACETONE;

EID: 2642588263     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je034160c     Document Type: Article

References (18)

1. McHugh, M. A.; Krukonis, V. J. Supercritical Fluid Extraction: Principles and Practice, 2nd ed.; Butterworth-Heinmann: Boston, 1994.
2. Eckert, C. A.; Knutson, B. L.; Debenedetti, P. G. Supercritical Fluids as Solvents for Chemical and Materials Processing. Nature 1996, 383, 313-318.
3. King, J. W.; Sahle-Demessie, E.; Temelli, F.; Teel, J. A. Thermal Gradient Fractionation of Glyceride Mixtures under Supercritical Fluid Conditions. J. Supercrit. Fluids 1997, 10, 127-137.
4. Jessop, P. G.; Leitner, W. Chemical Synthesis using Supercritical Fluids; Wiley-VCH: Meinheim, 1999.
5. Wittmann, K.; Wisniewski, W.; Mynott, R.; Leitner, W.; Kranemann, C. L.; Rische, T.; Eilbracht, P.; Kluwer: S.; Ernsting, J. M.; Elsevier: C. J. Rhodium-Catalyzed Hydroaminomethylation using Supercritical Carbon Dioxide as Solvent and Temporary Protecting Group. Chem.-Eur. J. 2001, 7, 4584-4589.
6. Cooper, A. I. Polymer Synthesis and Processing Using Supercritical Carbon Dioxide. J. Mater. Chem. 2000, 10, 207-234.
7. 2/Ethanol. Chem.-Eur. J. 2002, 8, 5593-5600.
8. Tochigi, 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.
9. Leu, A. H.; Robinson, D. B. Equilibrium Phase Properties of Selected Carbon Dioxide Binary Systems: n-Pentane-Carbon Dioxide and Isopentane-Carbon Dioxide. J. Chem. Eng. Data 1987, 32, 447-450.
10. Besserer, G. J.; Robinson, D. B. Equilibrium-Phase Properties of n-Pentane-Carbon Dioxide System. J. Chem. Eng. Data 1973, 18, 416-419.
11. Cheng, H.; Pozo de Fernandez, M. E.; Zollweg, J. A.; Streett, W. B. Vapor-Liquid Equilibrium in the System Carbon Dioxide + n-Pentane from 252 to 458 K at Pressures to 10 MPa. J. Chem. Eng. Data 1989, 34, 319-323.
12. Kiran, E.; Pohler, H.; Xiong, Y. Volumetric Properties of Pentane + Carbon Dioxide at High Pressures. J. Chem. Eng. Data 1996, 41, 158-165.
13. Pohler, H.; Kiran, E. Volumetric Properties of Carbon Dioxide + Acetone at High Pressures. J. Chem. Eng. Data 1997, 42, 379-383.
14. Bamberger, A.; Maurer, G. High-Pressure (Vapour + Liquid) Equilibria in (Carbon Dioxide + Acetone or 2-Propanol) at Temperatures from 293 K to 333 K. J. Chem. Thermodyn. 2000, 32, 685-700.
15. 2 + Acetone Systems in Various Phase Regions. J. Chem. Eng. Data 2003, 48, 1544-1548.
16. 2-Rich Region. Fluid Phase Equilib. 2001, 179, 131-138.
17. Lide, D. R. CRC Handbook of Chemistry and Physics, 73rd ed.; CRC Press: Boca Raton, FL, 1992-1993.
18. Eckert, C. A.; Ziger, D. H.; Johnston, K. P.; Kim, S. Solute Partial Molal Volumes in Supercritical Fluids. J. Phys. Chem. 1986, 90, 2738-2746.