A cubic equation of state with group contributions for the calculation of vapor-liquid equilibria of mixtures of hydrofluorocarbons and lubricant oils
Journal Article
·
· Industrial and Engineering Chemistry Research
- Univ. di Padova (Italy). Ist. di Impianti Chimici
- Chalmers Univ. of Technology, Gothenburg (Sweden). Dept. of Heat and Power Technology
A method for calculating the vapor-liquid equilibria of mixtures between hydrofluorocarbons and lubricant oils is presented. A cubic equation of state is used containing three parameters: the attractive on, a, the volume parameter, b, and the number of external degrees of freedom per molecule, c. To allow calculation of the parameters of the high molecular weight components, whose critical constants and vapor pressure are unknown, a group-contribution approach is developed for a, b, and c. The extension to mixtures is achieved by applying Huron-Vidal mixing rules. A modified Uniquac model is used to evaluate infinite-pressure activity coefficients. With the proposed method, the density of pure heavy components (such as n-hexadecane and pentaerythritol esters) is predicted as a function of temperature. Vapor-liquid equilibria calculations are presented for binary mixtures between several hydrofluorocarbons and pentaerythritol esters or hexadecane; a comparison with the results obtained by available models is also outlined.
- OSTI ID:
- 352675
- Journal Information:
- Industrial and Engineering Chemistry Research, Journal Name: Industrial and Engineering Chemistry Research Journal Issue: 5 Vol. 38; ISSN IECRED; ISSN 0888-5885
- Country of Publication:
- United States
- Language:
- English
Similar Records
Group-contribution equation of state for the prediction of vapor-liquid equilibria of mixtures containing hydrofluorocarbons and alkanes
Vapor-liquid equilibrium for methanol + 1,1-dimethylpropyl methyl ether at (288.15, 308.15, and 328.15) K
High-pressure phase equilibria for the carbon dioxide + 3-pentanol and carbon dioxide + 3-pentanol + water systems
Journal Article
·
Sat Aug 01 00:00:00 EDT 1998
· Industrial and Engineering Chemistry Research
·
OSTI ID:659051
Vapor-liquid equilibrium for methanol + 1,1-dimethylpropyl methyl ether at (288.15, 308.15, and 328.15) K
Journal Article
·
Wed May 01 00:00:00 EDT 1996
· Journal of Chemical and Engineering Data
·
OSTI ID:256900
High-pressure phase equilibria for the carbon dioxide + 3-pentanol and carbon dioxide + 3-pentanol + water systems
Journal Article
·
Sat May 01 00:00:00 EDT 1999
· Journal of Chemical and Engineering Data
·
OSTI ID:354426