Liquid-vapor and Solid-liquid-vapor Phase Equilibria in Natural Gas Systems
Title | Liquid-vapor and Solid-liquid-vapor Phase Equilibria in Natural Gas Systems PDF eBook |
Author | A. J. Kidnay |
Publisher | |
Pages | 35 |
Release | 1984 |
Genre | Natural gas |
ISBN |
Solid-liquid-vapor phase equilibria were measured for the binary systems carbon dioxide plus methane, carbon dioxide plus ethane, and carbon dioxide plus propane over the temperature region 204 to 216 K. Vapor-liquid phase equilibria were measured for carbon dioxide plus methane at 212 K, carbon dioxide plus ethane at 204, 209, and 212 K, and carbon dioxide plus propane at 216 K.
Liquid-vapor and Solid-liquid-vapor Equilibrium in Natural Gas Systems
Title | Liquid-vapor and Solid-liquid-vapor Equilibrium in Natural Gas Systems PDF eBook |
Author | E. Dendy Sloan |
Publisher | |
Pages | 101 |
Release | 1986* |
Genre | Carbon dioxide |
ISBN |
There were two major objectives for the work. The first objective was the experimental measurement and thermodynamic modeling of ternary vapor liquid equilibria of carbon dioxide systems of interest to the natural gas industry. The second objective was the measurement and thermodynamic modeling of solid-liquid-vapor phase behavior in binary carbon dixide systems.
Liquid-vapor and Solid-liquid-vapor Equilibrium in Natural Gas Systems
Title | Liquid-vapor and Solid-liquid-vapor Equilibrium in Natural Gas Systems PDF eBook |
Author | E. D. Sloan |
Publisher | |
Pages | 101 |
Release | 1983 |
Genre | Thermodynamic equilibrium |
ISBN |
Liquid-vapor Equilibria for Ternary Natural Gas Systems
Title | Liquid-vapor Equilibria for Ternary Natural Gas Systems PDF eBook |
Author | Colorado School of Mines |
Publisher | |
Pages | 83 |
Release | 1982 |
Genre | Chemical equilibria |
ISBN |
Vapor-liquid equilibria were measured for the binary systems methane + carbon dioxide at 230, 250, and 270 K; methane + ethane at 210, 230, 270 K; and ethane + carbon dioxide at 210, 213, 230, 250 K. The ternary stystem methane + ethane + carbon dioxide was studied at 230 K over the pressure range 1.15 MPa to 6.59 MPa. The Peng-Robinson equation of state was used to model the experimental data with an accuracy sufficient for most engineering calculations Preliminary studies were made of the solid-liquid-vapor equilibria for the binary systems methane + carbon dioxide and ethane + carbon dioxide.
Phase Equilibria and Gas Mixtures Properties
Title | Phase Equilibria and Gas Mixtures Properties PDF eBook |
Author | |
Publisher | |
Pages | |
Release | 1968 |
Genre | |
ISBN |
Solid-liquid-vapor Phase Equilibria in the Binary Systems
Title | Solid-liquid-vapor Phase Equilibria in the Binary Systems PDF eBook |
Author | Otto Robert Schweitzer |
Publisher | |
Pages | 322 |
Release | 1962 |
Genre | Phase rule and equilibrium |
ISBN |
Vapor-liquid Equilibria for a Helium-nitrogen-methane System
Title | Vapor-liquid Equilibria for a Helium-nitrogen-methane System PDF eBook |
Author | William Jefferson Boone |
Publisher | |
Pages | 28 |
Release | 1963 |
Genre | Phase rule and equilibrium |
ISBN |