Bubble point pressures of some selected carbon dioxide + synthetic C6+ mixtures

Journal of Chemical and Engineering Data

Volumn 43, Issue 5, 1998, Pages 785-788

  Shariati, Alireza ^b   Peters, Cor J ^a   Moshfeghian, Mahmood ^b  

^a DELFT UNIVERSITY OF TECHNOLOGY   (Netherlands)

^b SHIRAZ UNIVERSITY   (Iran)

Author keywords

[No Author keywords available]

Indexed keywords

BUBBLES (IN FLUIDS); CARBON DIOXIDE; CORRELATION METHODS; EQUATIONS OF STATE OF LIQUIDS;

BUBBLE POINT PRESSURES; CAILLETET APPARATUS; PENG-ROBINSON EQUATION OF STATE (PR EOS);

BINARY MIXTURES;

EID: 0032163152     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je970261x     Document Type: Article

References (5)

1. Aasberg-Petersen, K.; Stenby, E. Prediction of Thermodynamic Properties of Oil and Gas Condensate Mixtures. Ind. Eng. Chem. Res. 1991, 30, 248-254.
2. 30 Up to 1000 bar and 440 K. Fluid Phase Equilib. 1992, 73, 285-321.
3. Peng, D. Y.; Robinson, D. B. A New Two-Constant Equation of State. Ind. Eng. Chem. Fundam. 1976, 15, 59-64.
4. Peters, C. J.; de Roo, J. L.; de Swaan Arons, J. Measurements and Calculations of Phase Equilibria in Binary Mixtures of Propane + Tetratriacontane. Fluid Phase Equilib. 1992, 72, 251-266.
5. Peters, C. J.; de Roo, J. L.; de Swaan Arons, J. Phase Equilibria in Binary Mixtures of Propane and Hexacontane. Fluid Phase Equilib. 1993, 85, 301-312.