High-pressure phase equilibrium data for aromatic components of wine: Carbon dioxide/n-butanal system

Industrial and Engineering Chemistry Research

Volumn 39, Issue 11, 2000, Pages 4427-4430

  Da Silva, Marta Vázquez ^a   Barbosa, Domingos ^a  

^a UNIVERSITY OF PORTO   (Portugal)

Author keywords

[No Author keywords available]

Indexed keywords

ALDEHYDES; AROMATIC COMPOUNDS; ASSOCIATION REACTIONS; CARBON DIOXIDE; EQUATIONS OF STATE; HIGH PRESSURE EFFECTS; SOLUBILITY; SUPERCRITICAL FLUID EXTRACTION; WINE;

BUTANAL; HIGH PRESSURE PHASE EQUILIBRIUM; PENG-ROBINSON EQUATIONS OF STATE; SOAVE-REDLICH-KWONG EQUATIONS OF STATE;

PHASE EQUILIBRIA;

AROMATIC COMPOUND; BUTYRALDEHYDE; CARBON DIOXIDE;

ARTICLE; CALCULATION; EXTRACTION; PRESSURE; TEMPERATURE; WINE;

EID: 17544367636     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0002273     Document Type: Article

References (6)

1. Vázquez da Silva, M.; Barbosa, D.; Ferreira, P. O.; Mendonça, J. High-Pressure Phase Equilibrium Data for the Systems Carbon Dioxide/Ethyl Acetate and Carbon Dioxide/Isoamyl Acetate at 295.2, 303.2 and 313.3 K. Fluid Phase Equilib. 2000, in press.
2. Pereira, P. J.; Gomes de Azevedo, E. J. S.; Nunes da Ponte, M. Phase Equilibria for {2,3-Epoxypropanol (Glycidol) + Carbon Dioxide} from T = 292 K to T = 343 K at Pressures up to 27 MPa. J. Chem. Thermodyn. 1997, 29, 197.
3. Graboski, M. S.; Daubert, T. E. A Modified Soave Equation of State for Phase Equilibrium Calculations. 1. Hydrocarbon Systems. Ind. Eng. Chem. Process Des. Dev. 1978, 17, 443.
4. Peng, D. Y.; Robinson, D. B. A New Two-Constant Equation of State. Ind. Eng. Chem. Fundam. 1976, 15, 59.
5. Solórzano-Zavala, M.; Barrágan-Aroche, F.; Bazúa, E. R. Comparative Study of Mixing Rules for Cubic Equations of State in the Prediction of Multicomponent Vapor-Liquid Equilibria. Fluid Phase Equilib. 1996, 122, 99.
6. Yaws, C. L.; Chen, D.; Yang, H. C.; Tan, L.; Nico, D. Critical Properties of Chemicals. Hydrocarbon Process. 1989, 68, 61.