Roland Solimando - Academia.edu (original) (raw)
Papers by Roland Solimando
Http Www Theses Fr, 1991
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Fluid Phase Equilibria, 1997
... Article Outline. References. HaUlS[ EOglUDRIA ELSEVIER Fluid Phase Equilibria 134 (1997) 63... more ... Article Outline. References. HaUlS[ EOglUDRIA ELSEVIER Fluid Phase Equilibria 134 (1997) 6375 Phase equilibria modelling for binary systems that contain CO2 E. Cassel a, M. Matt a, M. Rogalski a.*, R ... Eng. Chem. 43 (1951) 25152520. [16] PK Behrens and SI Sandier ...
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Entropie, 1997
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Desalination and Water Treatment, 2015
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MATEC Web of Conferences, 2013
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Thermochimica Acta, 1997
... enthalpy at infinite dilution of NaC1 in water between 25C and 100C Nathalie Hubert*, Roland ... more ... enthalpy at infinite dilution of NaC1 in water between 25C and 100C Nathalie Hubert*, Roland Solimando, Alexandra Pere, Louis Schuffenecker Laboratoire de Thermodynamique des Sdparations, Ecole Nationale Sup ieure des Industries Chimiques, 1, Rue Grandville, BP 451 ...
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Thermochimica Acta, 2000
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Thermochimica Acta, 1999
ABSTRACT Solid–liquid equilibria (SLE) and formation of films at the air/water interface were inv... more ABSTRACT Solid–liquid equilibria (SLE) and formation of films at the air/water interface were investigated for binaries formed with 1-pyrenecarboxaldehyde (PCA) or fluorenone, mixed with pyrene or phenanthrene. In all systems studied, the components are non-miscible in the solid phase. Two eutectic points and the formation of a solid compound is observed in the diagram. The aggregation phenomena occurring in presence of water can lead to the formation of organized structures, similar to those observed in the case of surfactant/water systems. The results obtained suggest that these polyaromatic molecules have a tendency to stacking and agglomerating.
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Thermochimica Acta, 1992
ABSTRACT Five equations of state accurately expressing the vapor pressures of hydrocarbons were u... more ABSTRACT Five equations of state accurately expressing the vapor pressures of hydrocarbons were used to estimate ΔCp, the difference between liquid and ideal gas heat capacities. It was observed that two equations of state giving equally accurate vapor pressures can yield very different ΔCp estimates. The consequences are investigated and discussed.
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The Journal of Chemical Thermodynamics, 2002
ABSTRACT Dissolution enthalpies of anhydrous sodium sulfate in water were measured up to saturati... more ABSTRACT Dissolution enthalpies of anhydrous sodium sulfate in water were measured up to saturation atT= (287.8, 317.5, and 352.1) K with a SETARAM C80 mixing calorimeter. Experimental isotherms, and previous ones at T= 297.6 K and T= 317.5 K (Hubert, N. et al., Thermochim. Acta1995, 259, 41–48), all intersect around a molality of 2 mol · kg−1. These five isotherms have been fitted with the electrolyte-NRTL model according to a methodology presented in this paper. This methodology uses enthalpy values along with values atT= 298.15 K from the literature and leads to the proposal of a unique set of parameters that allows a simultaneous representation of dissolution enthalpies, apparent relative molar enthalpies, and osmotic coefficients of sodium sulfate in water. Very good agreement was obtained between experimental and calculated values of dissolution enthalpies and osmotic coefficients in (water + sodium sulfate).
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Oil & Gas Science and Technology, 1995
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Journal of Chemical & Engineering Data, 2003
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Journal of Chemical & Engineering Data, 2012
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Journal of Chemical & Engineering Data, 2000
ABSTRACT This paper is a continuation of our previous studies on thermodynamic properties of bina... more ABSTRACT This paper is a continuation of our previous studies on thermodynamic properties of binary systems formed by a long-chain n-alkane and a polyaromatic. Solid-liquid equilibrium and enthalpies of mixing data of the following systems were measured: {dibenzofuran (DBF) (CASRN 132-64-9), C12H8O + eicosane (CASRN 112-95-8), C20H42}, {DBF + pentacosane (CASRN 629-99-2), C25H52}, {DBF + octacosane (CASRN 630-02-4), C28H58}, {DBF + hexatriacontane (CASRN 630-08-6), C36H74}, {xanthene (CASRN 92-83-1), C13H10O + eicosane}, {xanthene + octacosane}, {xanthene + hexatriacontane}. All data were correlated using the group contribution model based on the lattice theory of Kehiahian et al. (J. Chim. Phys. 1978, 75, 1032-1048).
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Industrial & Engineering Chemistry Research, 2012
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Industrial & Engineering Chemistry Research, 2000
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Industrial & Engineering Chemistry Research, 1990
... Marek Rogalski, Bruno Carrier, Roland Solimando, and Andre Pikeloux* Laboratoire de Chimie-Ph... more ... Marek Rogalski, Bruno Carrier, Roland Solimando, and Andre Pikeloux* Laboratoire de Chimie-Physique, Facults des Sciences de Luminy, 13228 Marseille ... Plots of the octane vapor preessure deviations between the data given by the TRC Tables (1987) and those ob-tained ...
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Fluid Phase Equilibria, 1997
ABSTRACT Modelling of thermodynamic properties of chlorinated phenols in water and in 1-octane-ol... more ABSTRACT Modelling of thermodynamic properties of chlorinated phenols in water and in 1-octane-ol is presented. Activity coefficients at infinite dilution and enthalpies of mixing were considered. The UNIFAC method as presented by Gmehling et al. [J. Gmehling, J. Li, M. Schiller, A modified UNIFAC model: 2. Present parameter matrix and results for different thermodynamic properties, Ind. Eng. Chem. Res. 32 (1993) 178–193] and Larsen et al. [B.L. Larsen, P. Rasmussen, A. Fredenslund, A modified UNIFAC group-contribution model for prediction of phase equilibria and heats of mixing, Ind. Eng. Chem. Res. 26 (1987) 2274–2286] was used. A method combining the group contribution approach with correlation based on physical descriptors yields results within experimental error.
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Fluid Phase Equilibria, 2010
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Http Www Theses Fr, 1991
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Fluid Phase Equilibria, 1997
... Article Outline. References. HaUlS[ EOglUDRIA ELSEVIER Fluid Phase Equilibria 134 (1997) 63... more ... Article Outline. References. HaUlS[ EOglUDRIA ELSEVIER Fluid Phase Equilibria 134 (1997) 6375 Phase equilibria modelling for binary systems that contain CO2 E. Cassel a, M. Matt a, M. Rogalski a.*, R ... Eng. Chem. 43 (1951) 25152520. [16] PK Behrens and SI Sandier ...
Bookmarks Related papers MentionsView impact
Entropie, 1997
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Desalination and Water Treatment, 2015
Bookmarks Related papers MentionsView impact
Bookmarks Related papers MentionsView impact
MATEC Web of Conferences, 2013
Bookmarks Related papers MentionsView impact
Thermochimica Acta, 1997
... enthalpy at infinite dilution of NaC1 in water between 25C and 100C Nathalie Hubert*, Roland ... more ... enthalpy at infinite dilution of NaC1 in water between 25C and 100C Nathalie Hubert*, Roland Solimando, Alexandra Pere, Louis Schuffenecker Laboratoire de Thermodynamique des Sdparations, Ecole Nationale Sup ieure des Industries Chimiques, 1, Rue Grandville, BP 451 ...
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Thermochimica Acta, 2000
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Thermochimica Acta, 1999
ABSTRACT Solid–liquid equilibria (SLE) and formation of films at the air/water interface were inv... more ABSTRACT Solid–liquid equilibria (SLE) and formation of films at the air/water interface were investigated for binaries formed with 1-pyrenecarboxaldehyde (PCA) or fluorenone, mixed with pyrene or phenanthrene. In all systems studied, the components are non-miscible in the solid phase. Two eutectic points and the formation of a solid compound is observed in the diagram. The aggregation phenomena occurring in presence of water can lead to the formation of organized structures, similar to those observed in the case of surfactant/water systems. The results obtained suggest that these polyaromatic molecules have a tendency to stacking and agglomerating.
Bookmarks Related papers MentionsView impact
Thermochimica Acta, 1992
ABSTRACT Five equations of state accurately expressing the vapor pressures of hydrocarbons were u... more ABSTRACT Five equations of state accurately expressing the vapor pressures of hydrocarbons were used to estimate ΔCp, the difference between liquid and ideal gas heat capacities. It was observed that two equations of state giving equally accurate vapor pressures can yield very different ΔCp estimates. The consequences are investigated and discussed.
Bookmarks Related papers MentionsView impact
The Journal of Chemical Thermodynamics, 2002
ABSTRACT Dissolution enthalpies of anhydrous sodium sulfate in water were measured up to saturati... more ABSTRACT Dissolution enthalpies of anhydrous sodium sulfate in water were measured up to saturation atT= (287.8, 317.5, and 352.1) K with a SETARAM C80 mixing calorimeter. Experimental isotherms, and previous ones at T= 297.6 K and T= 317.5 K (Hubert, N. et al., Thermochim. Acta1995, 259, 41–48), all intersect around a molality of 2 mol · kg−1. These five isotherms have been fitted with the electrolyte-NRTL model according to a methodology presented in this paper. This methodology uses enthalpy values along with values atT= 298.15 K from the literature and leads to the proposal of a unique set of parameters that allows a simultaneous representation of dissolution enthalpies, apparent relative molar enthalpies, and osmotic coefficients of sodium sulfate in water. Very good agreement was obtained between experimental and calculated values of dissolution enthalpies and osmotic coefficients in (water + sodium sulfate).
Bookmarks Related papers MentionsView impact
Oil & Gas Science and Technology, 1995
Bookmarks Related papers MentionsView impact
Journal of Chemical & Engineering Data, 2003
Bookmarks Related papers MentionsView impact
Journal of Chemical & Engineering Data, 2012
Bookmarks Related papers MentionsView impact
Journal of Chemical & Engineering Data, 2000
ABSTRACT This paper is a continuation of our previous studies on thermodynamic properties of bina... more ABSTRACT This paper is a continuation of our previous studies on thermodynamic properties of binary systems formed by a long-chain n-alkane and a polyaromatic. Solid-liquid equilibrium and enthalpies of mixing data of the following systems were measured: {dibenzofuran (DBF) (CASRN 132-64-9), C12H8O + eicosane (CASRN 112-95-8), C20H42}, {DBF + pentacosane (CASRN 629-99-2), C25H52}, {DBF + octacosane (CASRN 630-02-4), C28H58}, {DBF + hexatriacontane (CASRN 630-08-6), C36H74}, {xanthene (CASRN 92-83-1), C13H10O + eicosane}, {xanthene + octacosane}, {xanthene + hexatriacontane}. All data were correlated using the group contribution model based on the lattice theory of Kehiahian et al. (J. Chim. Phys. 1978, 75, 1032-1048).
Bookmarks Related papers MentionsView impact
Industrial & Engineering Chemistry Research, 2012
Bookmarks Related papers MentionsView impact
Industrial & Engineering Chemistry Research, 2000
Bookmarks Related papers MentionsView impact
Industrial & Engineering Chemistry Research, 1990
... Marek Rogalski, Bruno Carrier, Roland Solimando, and Andre Pikeloux* Laboratoire de Chimie-Ph... more ... Marek Rogalski, Bruno Carrier, Roland Solimando, and Andre Pikeloux* Laboratoire de Chimie-Physique, Facults des Sciences de Luminy, 13228 Marseille ... Plots of the octane vapor preessure deviations between the data given by the TRC Tables (1987) and those ob-tained ...
Bookmarks Related papers MentionsView impact
Fluid Phase Equilibria, 1997
ABSTRACT Modelling of thermodynamic properties of chlorinated phenols in water and in 1-octane-ol... more ABSTRACT Modelling of thermodynamic properties of chlorinated phenols in water and in 1-octane-ol is presented. Activity coefficients at infinite dilution and enthalpies of mixing were considered. The UNIFAC method as presented by Gmehling et al. [J. Gmehling, J. Li, M. Schiller, A modified UNIFAC model: 2. Present parameter matrix and results for different thermodynamic properties, Ind. Eng. Chem. Res. 32 (1993) 178–193] and Larsen et al. [B.L. Larsen, P. Rasmussen, A. Fredenslund, A modified UNIFAC group-contribution model for prediction of phase equilibria and heats of mixing, Ind. Eng. Chem. Res. 26 (1987) 2274–2286] was used. A method combining the group contribution approach with correlation based on physical descriptors yields results within experimental error.
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Fluid Phase Equilibria, 2010
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