| # | Title | Journal | Year | Citations |
|---|
| 1 | SAFT: Equation-of-state solution model for associating fluids | Fluid Phase Equilibria | 1989 | 1,275 |
| 2 | A consistent correction for Redlich-Kwong-Soave volumes | Fluid Phase Equilibria | 1982 | 1,138 |
| 3 | Room temperature ionic liquids and their mixtures—a review | Fluid Phase Equilibria | 2004 | 1,135 |
| 4 | The isothermal flash problem. Part I. Stability | Fluid Phase Equilibria | 1982 | 1,024 |
| 5 | COSMO-RS: a novel and efficient method for the a priori prediction of thermophysical data of liquids | Fluid Phase Equilibria | 2000 | 1,002 |
| 6 | Group-contribution based estimation of pure component properties | Fluid Phase Equilibria | 2001 | 939 |
| 7 | New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures | Fluid Phase Equilibria | 1979 | 878 |
| 8 | The isothermal flash problem. Part II. Phase-split calculation | Fluid Phase Equilibria | 1982 | 681 |
| 9 | PSRK: A Group Contribution Equation of State Based on UNIFAC | Fluid Phase Equilibria | 1991 | 603 |
| 10 | Extension of the Peng-Robinson equation of state to complex mixtures: Evaluation of the various forms of the local composition concept | Fluid Phase Equilibria | 1983 | 597 |
| 11 | The solubility of solids in supercritical fluids | Fluid Phase Equilibria | 1999 | 439 |
| 12 | Solubility of CO2 in water from −1.5 to 100 °C and from 0.1 to 100 MPa: evaluation of literature data and thermodynamic modelling | Fluid Phase Equilibria | 2003 | 435 |
| 13 | A modified Huron-Vidal mixing rule for cubic equations of state | Fluid Phase Equilibria | 1990 | 419 |
| 14 | COSMO-RS as a tool for property prediction of IL mixtures—A review | Fluid Phase Equilibria | 2010 | 368 |
| 15 | Solubilities and diffusion coefficients of carbon dioxide and nitrogen in polypropylene, high-density polyethylene, and polystyrene under high pressures and temperatures | Fluid Phase Equilibria | 1999 | 346 |
| 16 | Phase diagram, latent heat, and specific heat of TBAB semiclathrate hydrate crystals | Fluid Phase Equilibria | 2005 | 335 |
| 17 | VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method | Fluid Phase Equilibria | 2004 | 330 |
| 18 | An internally consistent correlation for predicting the critical properties and molecular weights of petroleum and coal-tar liquids | Fluid Phase Equilibria | 1984 | 328 |
| 19 | Multicomponent phase equilibrium calculations for water–methanol–alkane mixtures | Fluid Phase Equilibria | 1999 | 306 |
| 20 | Group contribution methods for liquid mixtures: A critical review | Fluid Phase Equilibria | 1983 | 305 |
| 21 | Development of hydrophobic deep eutectic solvents for extraction of pesticides from aqueous environments | Fluid Phase Equilibria | 2017 | 303 |
| 22 | An overview of the mutual solubilities of water–imidazolium-based ionic liquids systems | Fluid Phase Equilibria | 2007 | 302 |
| 23 | Vapour–liquid equilibria in the carbon dioxide–water system, measurement and modelling from 278.2 to 318.2K | Fluid Phase Equilibria | 2004 | 299 |
| 24 | A speciation-based model for mixed-solvent electrolyte systems | Fluid Phase Equilibria | 2002 | 295 |
| 25 | Application of perturbation theory to a hard-chain reference fluid: an equation of state for square-well chains | Fluid Phase Equilibria | 2000 | 294 |
| 26 | Solubility and preferential solvation of indomethacin in 1,4-dioxane+water solvent mixtures | Fluid Phase Equilibria | 2010 | 285 |
| 27 | Low-pressure solubilities and thermodynamics of solvation of eight gases in 1-butyl-3-methylimidazolium hexafluorophosphate | Fluid Phase Equilibria | 2006 | 276 |
| 28 | A Flory–Huggins model based on the Hansen solubility parameters | Fluid Phase Equilibria | 2002 | 275 |
| 29 | The Lennard-Jones fluid: an accurate analytic and theoretically-based equation of state | Fluid Phase Equilibria | 1994 | 274 |
| 30 | High-pressure fluid-phase equilibria: Experimental methods and systems investigated (1988–1993) | Fluid Phase Equilibria | 1995 | 268 |
| 31 | Extension of the Ye and Shreeve group contribution method for density estimation of ionic liquids in a wide range of temperatures and pressures | Fluid Phase Equilibria | 2008 | 268 |
| 32 | On the derivation and extension of the uniquac equation | Fluid Phase Equilibria | 1978 | 262 |
| 33 | Peng-Robinson predictions for hydrocarbons, CO2, N2, and H2 S with pure water and NaCI brine | Fluid Phase Equilibria | 1992 | 262 |
| 34 | Hydrate formation in systems containing methane, ethane, propane, carbon dioxide or hydrogen sulfide in the presence of methanol | Fluid Phase Equilibria | 1985 | 261 |
| 35 | Solubility measurement and prediction of carbon dioxide in ionic liquids | Fluid Phase Equilibria | 2005 | 259 |
| 36 | A new form of the equation of state for pure substances and its application to oxygen | Fluid Phase Equilibria | 1985 | 258 |
| 37 | Ternary liquid–liquid equilibria for mixtures of toluene+n-heptane+an ionic liquid | Fluid Phase Equilibria | 2006 | 251 |
| 38 | Peng-Robinson equation of state: 40 years through cubics | Fluid Phase Equilibria | 2017 | 251 |
| 39 | Gas storage in structure H hydrates | Fluid Phase Equilibria | 1998 | 249 |
| 40 | Estimation of pure component properties | Fluid Phase Equilibria | 2008 | 249 |
| 41 | Improvements of COSMO-SAC for vapor–liquid and liquid–liquid equilibrium predictions | Fluid Phase Equilibria | 2010 | 249 |
| 42 | Group-contribution+ (GC+) based estimation of properties of pure components: Improved property estimation and uncertainty analysis | Fluid Phase Equilibria | 2012 | 249 |
| 43 | Mechanisms of gas hydrate formation and inhibition | Fluid Phase Equilibria | 2002 | 244 |
| 44 | Solubilities of carbon dioxide and nitrogen in polystyrene under high temperature and pressure | Fluid Phase Equilibria | 1996 | 243 |
| 45 | A group contribution method for viscosity estimation of ionic liquids | Fluid Phase Equilibria | 2008 | 242 |
| 46 | Hydrate phase equilibria of the guest mixtures containing CO2, N2 and tetrahydrofuran | Fluid Phase Equilibria | 2001 | 240 |
| 47 | Prediction of vapor-liquid equilibrium with the LCVM model: a linear combination of the Vidal and Michelsen mixing rules coupled with the original UNIF | Fluid Phase Equilibria | 1994 | 239 |
| 48 | Thermophysical properties of n-Alkanes from C1 to C20 and their prediction for higher ones | Fluid Phase Equilibria | 1990 | 233 |
| 49 | The friction theory (f-theory) for viscosity modeling | Fluid Phase Equilibria | 2000 | 233 |
| 50 | Estimation of pure component properties | Fluid Phase Equilibria | 2004 | 233 |
