Industrial applications of cubic equations of state for VLE calculations, with emphasis on H2 systems
- 31 December 1983
- journal article
- Published by Elsevier in Fluid Phase Equilibria
- Vol. 13, 59-76
- https://doi.org/10.1016/0378-3812(83)80082-x
Abstract
No abstract availableThis publication has 22 references indexed in Scilit:
- Phase Equilibria in the H2/C2H4System at Temperatures from 114.1 to 247.1 K and Pressures to 600 MPaBerichte der Bunsengesellschaft für physikalische Chemie, 1983
- A novel apparatus for the measurement of the phase and volumetric behavior at high temperatures and pressures and its application to study VLE in the hydrogen-tetralin systemFluid Phase Equilibria, 1981
- Gas-liquid equilibrium in hydrogen + n-hexadecane and methane + n-hexadecane at elevated temperatures and pressuresJournal of Chemical & Engineering Data, 1980
- Modified Soave Equation of State for Phase Equilibrium CalculationsIndustrial & Engineering Chemistry Process Design and Development, 1980
- Gas—liquid equilibrium in hydrogen + tetralin + diphenylmethane and hydrogen + tetralin + m-xyleneFluid Phase Equilibria, 1979
- A Modified Soave Equation of State for Phase Equilibrium Calculations. 3. Systems Containing HydrogenIndustrial & Engineering Chemistry Process Design and Development, 1979
- A Modified Soave Equation of State for Phase Equilibrium Calculations. 2. Systems Containing CO2, H2S, N2, and COIndustrial & Engineering Chemistry Process Design and Development, 1978
- A Modified Soave Equation of State for Phase Equilibrium Calculations. 1. Hydrocarbon SystemsIndustrial & Engineering Chemistry Process Design and Development, 1978
- Solubilities of gases in liquids at elevated temperatures. Henry's constants for hydrogen, methane, and ethane in hexadecane, bicyclohexyl, and diphenylmethaneThe Journal of Physical Chemistry, 1972
- Vapor-Liquid Equilibria at High Pressures. Vapor-Phase Fugacity Coefficients in Nonpolar and Quantum-Gas MixturesIndustrial & Engineering Chemistry Fundamentals, 1967