Improved Modeling of the Phase Behavior of Asymmetric Hydrocarbon Mixtures with the Peng−Robinson Equation of State Using a Different Temperature Dependency of the Parameter a
- 18 March 1998
- journal article
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 37 (5), 1651-1662
- https://doi.org/10.1021/ie970644o
Abstract
No abstract availableKeywords
This publication has 28 references indexed in Scilit:
- High-Pressure Phase Equilibria in the Binary System (Methane + 5-α-Cholestane)Journal of Chemical & Engineering Data, 1997
- An Approach for the Application of a Cubic Equation of State to Hydrogen−Hydrocarbon SystemsIndustrial & Engineering Chemistry Research, 1996
- High pressure-high temperature reservoir fluids: investigation of synthetic condensate gases containing a solid hydrocarbonFluid Phase Equilibria, 1995
- Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal AlkanesJournal of Chemical & Engineering Data, 1995
- Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic HydrocarbonsJournal of Chemical & Engineering Data, 1995
- A new generalized alpha function for a cubic equation of state Part 1. Peng-Robinson equationFluid Phase Equilibria, 1995
- Phase Equilibria of Alkanes in Natural Gas Systems. 1. Alkanes in MethaneJournal of Chemical & Engineering Data, 1995
- High‐pressure vapor‐liquid equilibrium with a UNIFAC‐based equation of stateAIChE Journal, 1990
- Phase equilibria of (methane + n-hexadecane) and (p, Vm, T) of n-hexadecaneThe Journal of Chemical Thermodynamics, 1985
- A New Two-Constant Equation of StateIndustrial & Engineering Chemistry Fundamentals, 1976