An automated apparatus for equilibrium phase compositions, densities, and interfacial tensions: Data for carbon dioxide + decane

Fluid Phase Equilibria

Volumn 179, Issue 1-2, 2001, Pages 43-66

  Shaver, R D ^a   Robinson Jr , R L ^a   Gasem, K A M ^a  

^a Oklahoma State University   (United States)

Author keywords

Carbon dioxide; Decane; Interfacial tension; Phase densities; Phase equilibrium

Indexed keywords

AUTOMATION; DENSITY OF LIQUIDS; FLUIDS; SURFACE TENSION;

LIQUID PHASE COMPOSITIONS;

PHASE EQUILIBRIA;

CARBON DIOXIDE; DECANE;

CARBON DIOXIDE; DENSITY; FLUID INTERFACE; PARAFFIN; VAPOR-LIQUID EQUILIBRIUM;

APPARATUS; ARTICLE; AUTOANALYSIS; COMPUTER SYSTEM; DENSITY; DRUG MIXTURE; PHASE TRANSITION; PHYSICS; PRESSURE; TECHNIQUE; THERMODYNAMICS; VAPOR;

EID: 0035946150     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0378-3812(00)00475-1     Document Type: Article

References (25)

1. Evaluation of the simplified perturbed hard chain theory (SPHCT) for prediction of phase behavior of n-paraffins and mixtures of n-paraffins with ethane
2. 2-hydrocarbon systems
3. Application of the simplified-perturbed-hard-chain theory for pure components near the critical point
4. 2 + n-butane
5. 2 + n-decane
6. 2 + n-tetradecane
7. 2 + benzene
8. 2 + n-butane + decane
9. An efficient method for the determination of interfacial tensions from drop profiles
10. 2 system
11. 2/decane/tetralin at 71.1 and 104.4°C
12. Critical exponents from field theory
13. Determination of critical exponents from measurements of binary vapor-liquid equilibrium in the neighborhood of the critical line
14. Application of the Wilson-Wegner expansion to represent vapor-liquid equilibrium surfaces of binary and ternary systems from the critical locus to the vapor pressure of the heavier component
15. Corrections to scaling laws