A comment on water’s structure using monomer fraction data and theories

Capabilities and Limitations of an Association Theory for Chemicals in Liquid or Supercritical Solvents

Dimerization of Carboxylic Acids: An Equation of State Approach.

scientific article published on 14 February 2017

Electrospun fiber mats containing shikonin and derivatives with potential biomedical applications

scientific article published on 21 February 2011

Equation of state modelling of systems with ionic liquids: Literature review and application with the Cubic Plus Association (CPA) model

article

Evaluation of the Nonrandom Hydrogen Bonding (NRHB) Theory and the Simplified Perturbed-Chain-Statistical Associating Fluid Theory (sPC-SAFT). 2. Liquid−Liquid Equilibria and Prediction of Monomer Fraction in Hydrogen Bonding Systems

Evaluation of the Nonrandom Hydrogen Bonding (NRHB) Theory and the Simplified Perturbed-Chain−Statistical Associating Fluid Theory (sPC-SAFT). 1. Vapor−Liquid Equilibria

Experimental determination and modeling of the phase behavior for the direct synthesis of dimethyl carbonate from methanol and carbon dioxide

Experimental determination and modeling of the phase behavior for the selective oxidation of benzyl alcohol in supercritical CO2

Experimental study and phase equilibrium modeling of systems containing acid gas and glycol

Modeling Phase Equilibria for Acid Gas Mixtures using the Cubic-Plus-Association Equation of State. 3. Applications Relevant to Liquid or Supercritical CO2 Transport

Modeling Water Containing Systems with the Simplified PC-SAFT and CPA Equations of State

Modeling of phase equilibria with CPA using the homomorph approach

article published in 2011

Modeling phase equilibria for acid gas mixtures using the CPA equation of state. I. Mixtures with H2S

Modeling phase equilibria for acid gas mixtures using the CPA equation of state. Part II: Binary mixtures with CO2

Modeling phase equilibria for acid gas mixtures using the CPA equation of state. Part IV. Applications to mixtures of CO2 with alkanes

Modeling systems relevant to the biodiesel production using the CPA equation of state

article published in 2016

Modeling the phase behavior in mixtures of pharmaceuticals with liquid or supercritical solvents.

scientific article published in May 2009

Modeling the solid-liquid equilibrium in pharmaceutical-solvent mixtures: Systems with complex hydrogen bonding behavior

Modeling the vapor–liquid equilibria of polymer–solvent mixtures: Systems with complex hydrogen bonding behavior

Modelling phase equilibria for acid gas mixtures using the CPA equation of state. Part V: Multicomponent mixtures containing CO2 and alcohols

article published in 2015

Modelling phase equilibria for acid gas mixtures using the CPA equation of state. Part VI. Multicomponent mixtures with glycols relevant to oil and gas and to liquid or supercritical CO 2 transport applications

On the predictive capabilities of CPA for applications in the chemical industry: Multicomponent mixtures containing methyl-methacrylate, dimethyl-ether or acetic acid

Phase Equilibria of Mixtures Containing Organic Sulfur Species (OSS) and Water/Hydrocarbons: VLE Measurements and Modeling Using the Cubic-Plus-Association Equation of State

Phase Equilibria of Three Binary Mixtures: Methanethiol + Methane, Methanethiol + Nitrogen, and Methanethiol + Carbon Dioxide

Phase Equilibrium Measurements and Modeling of 1-Propanethiol +1-Butanethiol + CH4 in Methane Ternary System at 303, 336, and 368 K and Pressure Up to 9 MPa

Process Design of Industrial Triethylene Glycol Processes Using the Cubic-Plus-Association (CPA) Equation of State

Selective oxidation of benzyl alcohol in dense CO2: Insight by phase behavior modeling

The role of monomer fraction data in association theories—Can we improve the performance for phase equilibrium calculations?

Towards predictive association theories

Use of monomer fraction data in the parametrization of association theories

Vapor–Liquid–Liquid Equilibrium Measurements and Modeling of Ethanethiol + Methane + Water, 1-Propanethiol + Methane + Water and 1-Butanethiol + Methane + Water Ternary Systems at 303, 335, and 365 K and Pressure Up to 9 MPa

Vapor–Liquid–Liquid Equilibrium Measurements and Modeling of the Methanethiol + Methane + Water Ternary System at 304, 334, and 364 K