Automatic generation of global phase equilibrium diagrams for binary systems from equations of state-Reference-Cited by-同舟云学术

Automatic generation of global phase equilibrium diagrams for binary systems from equations of state

Published:2009-11 Issue:11 Volume:33 Page:1793-1804
ISSN:0098-1354
Container-title:Computers & Chemical Engineering
language:en
Short-container-title:Computers & Chemical Engineering

Author:

Patel Keyur S.,Sunol Aydin K.

Publisher

Elsevier BV

Subject

Computer Science Applications,General Chemical Engineering

Reference25 articles.

1. Predictions of critical behavior using the Wong–Sandler mixing rule;Alvarado;Journal of Supercritical Fluids,1998

2. Reliable computation of binary homogeneous azeotropes of multi-component mixtures at higher pressures through equation of states;Aslam;Fluid Phase Equilibria,2004

3. Critical points with the Wong–Sandler mixing rule. I. Calculations with the van der Waals equation of state;Castier;Chemical Engineering Science,1997

4. Critical points with the Wong–Sandler mixing rule. II. Calculations with a modified Peng–Robinson equation of state;Castier;Chemical Engineering Science,1997

5. Global phase equilibrium calculations: Critical lines, critical end points and liquid–liquid–vapour equilibrium in binary mixtures;Cismondi;Journal of Supercritical Fluids,2007

Cited by 12 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. Modeling of solid-fluid equilibria of pure n-alkanes and binary methane + n-alkane systems through predictive correlations;The Journal of Supercritical Fluids;2020-12

2. Azeotrope-Breaking Potential of Binary Mixtures in Phase Equilibria Modeling;Distillation - Modelling, Simulation and Optimization;2019-12-04

3. Second-Order Differential Accelerators Based on the Geometry of Equilibrium for Thermodynamic Calculations. Part I. Pure Fluids;Industrial & Engineering Chemistry Research;2019-10-21

4. SUBSTITUTION OF SOLVENTS BY SAFER PRODUCTS;Handbook of Solvents;2019

5. Calculation of critical points from Helmholtz-energy-explicit mixture models;Fluid Phase Equilibria;2017-02