Zobrazeno 1 - 10
of 15
pro vyhledávání: '"Joan Escandell"'
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:
Fluid Phase Equilibria
Fluid Phase Equilibria, Elsevier, 2014, 362 (25), pp.87-95. ⟨10.1016/j.fluid.2013.09.009⟩
Fluid Phase Equilibria, 2014, 362 (25), pp.87-95. ⟨10.1016/j.fluid.2013.09.009⟩
Fluid Phase Equilibria, Elsevier, 2014, 362 (25), pp.87-95. ⟨10.1016/j.fluid.2013.09.009⟩
Fluid Phase Equilibria, 2014, 362 (25), pp.87-95. ⟨10.1016/j.fluid.2013.09.009⟩
International audience; The accurate prediction of high pressure phase equilibria is crucial for the development and the design of chemical engineering processes. Among them the modeling of complex systems, such as petroleum fluids with water, has be
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::9bc14a1ae53548f2865e845cc6c45c76
https://hal.archives-ouvertes.fr/hal-00872639/file/FluidPhaseEquilibria2013.pdf
https://hal.archives-ouvertes.fr/hal-00872639/file/FluidPhaseEquilibria2013.pdf
Publikováno v:
Fluid Phase Equilibria
Fluid Phase Equilibria, Elsevier, 2011, 301 (1), pp.80-97. ⟨10.1016/j.fluid.2010.11.009⟩
Fluid Phase Equilibria, 2011, 301 (1), pp.80-97. ⟨10.1016/j.fluid.2010.11.009⟩
Fluid Phase Equilibria, Elsevier, 2011, 301 (1), pp.80-97. ⟨10.1016/j.fluid.2010.11.009⟩
Fluid Phase Equilibria, 2011, 301 (1), pp.80-97. ⟨10.1016/j.fluid.2010.11.009⟩
International audience; A generalized NRTL model was previously proposed for the modeling of non ideal systems and was extended to the prediction of phase equilibria under pressure according to the cubic NRTL-PR EoS. In this work, the model is reform
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::92e21ca0dfd3403fcb632c09c1c52c32
https://hal.archives-ouvertes.fr/hal-01464747
https://hal.archives-ouvertes.fr/hal-01464747
Publikováno v:
Chemical Engineering Science
Chemical Engineering Science, Elsevier, 2011, 66 (18), pp.4148-4156. ⟨10.1016/j.ces.2011.05.043⟩
Chemical Engineering Science, Elsevier, 2011, 66 (18), pp.4148-4156. ⟨10.1016/j.ces.2011.05.043⟩
International audience; This paper describes an EoS/GE approach based on cubic equations of state making reference to low pressure GE models derived from the lattice fluid theory of Guggenheim. The proposed method does not present the theoretical pro
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::bab3a1bf1065366e42490057fbb8b75a
https://hal.archives-ouvertes.fr/hal-01023163/file/ENJE.pdf
https://hal.archives-ouvertes.fr/hal-01023163/file/ENJE.pdf
Publikováno v:
Industrial and engineering chemistry research
Industrial and engineering chemistry research, American Chemical Society, 2010, 49 (16), pp.7580-7588. ⟨10.1021/ie100121c⟩
Industrial and engineering chemistry research, 2010, 49 (16), pp.7580-7588. ⟨10.1021/ie100121c⟩
Industrial and engineering chemistry research, American Chemical Society, 2010, 49 (16), pp.7580-7588. ⟨10.1021/ie100121c⟩
Industrial and engineering chemistry research, 2010, 49 (16), pp.7580-7588. ⟨10.1021/ie100121c⟩
International audience; The topic of the present work is the development of a simple model for the description of phase equilibria occurring in nonideal systems, such as those containing size-asymmetric components or mixtures made of polar or associa
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::d895a18d4cda5f7af8118026e24e200a
https://hal.archives-ouvertes.fr/hal-01025255
https://hal.archives-ouvertes.fr/hal-01025255
Publikováno v:
Journal of Chemical & Engineering Data; Dec2010, Vol. 55 Issue 12, p5449-5452, 4p