Zobrazeno 1 - 10
of 69
pro vyhledávání: '"Evelyne Neau"'
Publikováno v:
Industrial and engineering chemistry research
Industrial and engineering chemistry research, American Chemical Society, 2021, 60 (30), pp.11513-11524. ⟨10.1021/acs.iecr.1c01545⟩
Industrial and engineering chemistry research, 2021, 60 (30), pp.11513-11524. ⟨10.1021/acs.iecr.1c01545⟩
Industrial and engineering chemistry research, American Chemical Society, 2021, 60 (30), pp.11513-11524. ⟨10.1021/acs.iecr.1c01545⟩
Industrial and engineering chemistry research, 2021, 60 (30), pp.11513-11524. ⟨10.1021/acs.iecr.1c01545⟩
International audience; Further to the Part I of the present paper, the second Part is concentrated around the VLE modeling of binary mixtures involving the three glycol ethers previously studied experimentally. The authors propose to use the NRTL-PR
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::66e797d7d5843957070b5e0a4c625d6e
https://hal.archives-ouvertes.fr/hal-03379757/document
https://hal.archives-ouvertes.fr/hal-03379757/document
Autor:
Evelyne Neau, Isabelle Raspo
Publikováno v:
Fluid Phase Equilibria
Fluid Phase Equilibria, Elsevier, 2020, 506, pp.112371. ⟨10.1016/j.fluid.2019.112371⟩
Fluid Phase Equilibria, 2020, 506, pp.112371. ⟨10.1016/j.fluid.2019.112371⟩
Fluid Phase Equilibria, Elsevier, 2020, 506, pp.112371. ⟨10.1016/j.fluid.2019.112371⟩
Fluid Phase Equilibria, 2020, 506, pp.112371. ⟨10.1016/j.fluid.2019.112371⟩
International audience; Relative permittivity, also known as static dielectric constant, is a key property of solvents in electrolyte solutions. It strongly influences the solubility of solutes and, therefore, it can be used as a predictive tool in c
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::7c4c6bf5ca951ae88e2a26675866daf2
https://hal.archives-ouvertes.fr/hal-02325903/document
https://hal.archives-ouvertes.fr/hal-02325903/document
Publikováno v:
Fluid Phase Equilibria
Fluid Phase Equilibria, Elsevier, 2018, 458, pp.194-210. ⟨10.1016/j.fluid.2017.09.028⟩
Fluid Phase Equilibria, 2018, 458, pp.194-210. ⟨10.1016/j.fluid.2017.09.028⟩
Fluid Phase Equilibria, Elsevier, 2018, 458, pp.194-210. ⟨10.1016/j.fluid.2017.09.028⟩
Fluid Phase Equilibria, 2018, 458, pp.194-210. ⟨10.1016/j.fluid.2017.09.028⟩
International audience; The offshore exploitation of petroleum fluids in normal conditions of pressure and temperature of transport and in presence of salt water is concerned with the prevention of gas hydrate formation, generally thanks to continuou
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::14884de5652d6da9acfe797c964f0846
https://hal.archives-ouvertes.fr/hal-01703014/document
https://hal.archives-ouvertes.fr/hal-01703014/document
Publikováno v:
Fluid Phase Equilibria
Fluid Phase Equilibria, 2016, 427, pp.126-142. ⟨10.1016/j.fluid.2016.06.035⟩
Fluid Phase Equilibria, Elsevier, 2016, 427, pp.126-142. ⟨10.1016/j.fluid.2016.06.035⟩
Fluid Phase Equilibria, 2016, 427, pp.126-142. ⟨10.1016/j.fluid.2016.06.035⟩
Fluid Phase Equilibria, Elsevier, 2016, 427, pp.126-142. ⟨10.1016/j.fluid.2016.06.035⟩
The goal of this study is to propose a modification of the NRTL-PR EoS for the prediction of phase equilibria and excess enthalpies in mixtures containing methanol with hydrocarbons; indeed, with these systems, the original equation is confronted to
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::825d1eac75fec7efaf13a98379145121
https://hal.science/hal-01369874/document
https://hal.science/hal-01369874/document
Publikováno v:
Journal of Chemical & Engineering Data. 55:5449-5452
In this study, infinite dilution diffusion coefficients of aromatic compounds in ternary mixtures were measured at 298.15 K using the Taylor dispersion technique. The experimental data of benzene i...
Publikováno v:
Industrial and engineering chemistry research
Industrial and engineering chemistry research, 2010, 49 (16), pp.7589-7596. ⟨10.1021/ie101266x⟩
Industrial and engineering chemistry research, American Chemical Society, 2010, 49 (16), pp.7589-7596. ⟨10.1021/ie101266x⟩
Industrial and engineering chemistry research, 2010, 49 (16), pp.7589-7596. ⟨10.1021/ie101266x⟩
Industrial and engineering chemistry research, American Chemical Society, 2010, 49 (16), pp.7589-7596. ⟨10.1021/ie101266x⟩
International audience; The purpose of this study is to propose a simple cubic equation of state for the prediction of phase equilibria in highly non ideal systems. The NRTL-PR equation of state is based on the association of the Peng−Robinson EoS
Publikováno v:
Fluid Phase Equilibria. 276:156-164
Cubic equations of state (EoS) are commonly used for industrial applications, due to their simplicity in predicting pure compound and mixture thermodynamic properties in vapor and liquid phases. The accuracy of their predictions mainly depends on the
Publikováno v:
Fluid Phase Equilibria. 276:87-93
A theoretical analysis of the strengths and weaknesses of the Soave, Twu and Boston–Mathias attractive terms was performed with the Redlich–Kwong EoS. Special attention was paid to the variations of the alpha functions and their first and second
Publikováno v:
Journal of Chemical & Engineering Data. 53:444-448
Diffusion coefficients of aromatic compounds at infinite dilution in binary mixtures have been measured at 298.15 K with respect to composition using the Taylor dispersion technique. The binary mixtures considered in this work were from alcohols (met
Publikováno v:
Journal of Chemical & Engineering Data. 52:977-981
The Taylor dispersion technique was used to measure the diffusion coefficients of benzene, chlorobenzene, ethylbenzene, toluene, p-chlorotoluene, naphthalene, pyrene, and perylene at infinite dilution in mixtures of hexane + octane, hexane + decane,