Peng-Robinson predictions for hydrocarbons, CO2, N2, and H2 S with pure water and NaCI brine-Reference-Cited by-同舟云学术

Peng-Robinson predictions for hydrocarbons, CO2, N2, and H2 S with pure water and NaCI brine

Published:1992-09 Issue: Volume:77 Page:217-240
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Søreide Ingolf,Whitson Curtis H.

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference40 articles.

1. Solubility of methane in brines from 0 to 300°C;Cramer;Ind. Eng. Chem. Process Des. Dev.,1984

2. Phase Equilibria in Hydrocarbon-Water Systems. II The solubility of ethane in water at pressures to 10,000 psi;Culberson;Trans. AIME,1950

3. Phase equilibria in hydrocarbon-water systems. III The solubility of methane in water at pressures to 10,000 psi;Culberson;Trans. AIME,1951

4. Pressure-volume-temperature and solubility relations for natural gas-water mixtures;Dodson,1944

5. Gillespie P.C., Owens J.L. and Wilson G.M., Sour water equilibria extended to high temperatures and with inerts present. Paper No. 34b presented at the AIChE Winter National Meeting, Atlanta, GA, March 11–14. 1984

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