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Dive into the research topics where Jacques Schwartzentruber is active.

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Featured researches published by Jacques Schwartzentruber.


Geochimica et Cosmochimica Acta | 1987

Dissolution of quartz into dilute alkaline solutions at 90°C: A kinetic study

Jacques Schwartzentruber; Walter Fürst; H. Renon

Abstract The rate of dissolution of Fontainebleau sand (pure quartz) into sodium hydroxide solutions (from 0.001 M to 0.5 M) has been determined at 90°C in well-stirred vessels. Dissolution leads to an equilibrium state, controlled by the solubility of quartz in pure water as undissociated silicic acid H4SiO4. As long as the initial molality of sodium hydroxide does not exceed 0.02 mol · kg−1, the dissolution leads only to the formation of the three monomeric species H4SiO4, H3SiO4− and H2SiO42−, while polymers appear in the silica-rich solutions obtained in more alkaline media. The rate of dissolution can be represented by an adaptation of Stobers model to alkaline solutions; the basic assumption is that the quartz surface is partially covered by a layer of adsorbed silicate ions, which represent an intermediate species between solid and dissolved silica.


Fluid Phase Equilibria | 1987

Representation of the vaporliquid equilibrium of the ternary system carbon dioxide propane methanol and its binaries with a cubic equation of state : a new mixing rule

Jacques Schwartzentruber; Francine Galivel-Solastiouk; H. Renon

Abstract Erroneous liquid phase splitting is often predicted when correlating the vapor-liquid equilibrium of alcohol-alkane systems with a cubic equation of state. It is shown that even the local-composition mixing rules are not sufficiently flexible for an accurate representation of the propane-methanol system, and a new empirical three-parameter mixing rule is introduced. The ternary system carbon-dioxide - propane - methanol is well-predicted from the binary data.


Fluid Phase Equilibria | 1996

Modeling of multiphase liquid equilibria for multicomponent mixtures

Fernando García-Sánchez; Jacques Schwartzentruber; Mohamed Naceur Ammar; H. Renon

Abstract A computational procedure to correlate multicomponent, multiphase liquid equilibria in terms of excess Gibbs energy models is described. This includes an efficient hybrid algorithm for solving the multiphase liquid equilibria flash problem which is an extension of the approach proposed by Ammar and Renon to perform vapor-liquid flash calculations. The algorithms presented in this work for the calculation of multiphase liquid equilibria, the themodynamic stability test based on the tangent plan criterion, as described by Michelsen, and the methods for estimation of interaction parameters of the NRTL, UNIQUAC, and extended UNIQUAC models, were tested on the representation of experimental two- and three-liquid phase equilibrium data of ternary and quaternary mixtures. Agreement between calculated and measured equilibrium data was excellent for most systems studied.


Fluid Phase Equilibria | 1991

Equations of state: how to reconcile flexible mixing rules, the virial coefficient constraint and the “michelsen-Kistenmacher syndrome” for multicomponent systems

Jacques Schwartzentruber; H. Renon

Schwartzentruber J. and Renon H., 1991. Equations of state: how to reconcile flexible mixing rules, the virial coefficient constraint and the “Michelsen-Kistenmacher syndrome” for multicomponent systems. Fluid Phase Equilibria, 677: 99-110. Non-quadratic mixing rules in the attractive parameter of a cubic equation of state are very effective for the correlation of phase behaviour of strongly non-ideal systems. However, these mixing rules are not consistent with the second virial coefficient being a quadratic function of mole fractions. Recently, Michelsen and Kistenmacher pointed out other drawbacks of some of these mixing rules. In this paper, we present a new formulation of such mixing rules which avoids these problems, and a simple form of the density-dependency of the mixing rules which keeps the cubic form of the equation of state, while ensuring consistency with the second virial constraint.


Fluid Phase Equilibria | 1989

New determinations of high pressure vapor-liquid equilibria in binary systems containing n-propylbenzene with nitrogen or carbon dioxide consistent with the Prausnitz-Keeler test

H. Renon; Serge Laugier; Jacques Schwartzentruber; Dominique Richon

The test of Prausnitz and Keeler consists of plots, or linear regression derived from the equality of fugacities of the heavy component in the liquid and vapor phases, giving the cross second and third virial coefficients. Its application resulted in improvement of the capillary sampling static method of measurements of P,x,y,T data and showed the consistency of new data for the systems of propylbenzene with CO2 and N2 obtained by five different experimental methods, including four static methods with three different sampling techniques, and one variable volume cell and one dynamic method.


Biotechnology and Bioengineering | 2000

Protein precipitation by caprylic acid: Equilibrium composition data

Nadine Bernard; Claude Jolivalt; Jacques Schwartzentruber

The precipitation equilibria of hen egg‐white lysozyme and bovine serum albumin from aqueous solutions by caprylic acid were studied. A thermodynamic equilibrium was obtained, and the compositions of both the precipitate and the aqueous phases were measured to establish phase diagrams for both systems. The precipitate was not pure protein, but also contained large amounts of water and caprylic acid. At constant initial pH and ionic strength, the composition of both phases depended only on the overall composition of the system. This suggests that protein precipitation by fatty acids should be pictured as liquid–liquid rather than solid–liquid equilibria. The precipitated proteins retained high biological activity.


Industrial & Engineering Chemistry Research | 1989

Extension of UNIFAC to high pressures and temperatures by the use of a cubic equation of state

Jacques Schwartzentruber; Henri Renon


Industrial & Engineering Chemistry Process Design and Development | 1986

Prediction of the binary parameters of a cubic equation of state from a group-contribution method

Jacques Schwartzentruber; Luis Ponce-Ramirez; Henri Renon


Symposium on thermophysical properties for industrial process design -AICHE Spring national meeting | 1994

Regression of complex phase equilibrium data : thermodynamic modeling of microemulsion phase diagrams

Jacques Schwartzentruber; Fernando Garcia Sanchez; Henri Renon


6ème Congrès français de génie des procédés | 1997

Précipitation des protéines par des acides gras : modélisation des équilibres entre phases

N. Bernard; Claude Jolivalt; Jacques Schwartzentruber

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H. Renon

École Normale Supérieure

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Claude Jolivalt

École Normale Supérieure

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Nadine Bernard

École Normale Supérieure

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Serge Laugier

École Normale Supérieure

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