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  4. 1997
Showing papers on "Activity coefficient published in 1997"
Journal Article•10.1016/S0016-7037(97)00128-2•
Evaluation of internally consistent parameters for the triple-layer model by the systematic analysis of oxide surface titration data

[...]

Nita Sahai1, Dimitri A. Sverjensky1•
Johns Hopkins University1
01 Jul 1997-Geochimica et Cosmochimica Acta
TL;DR: Sahai et al. as mentioned in this paper performed a systematic analysis of surface titration data from the literature for ten oxides (anatase, hematite, goethite, rutile, amorphous silica, quartz, magnetite, δ-MnO2, corundum, and γ-alumina) in ten electrolytes (LiNo3, Na NO3, KNO3, CsNO3), over a wide range of ionic strengths (0.001 M-2.9 M) to establish adsorption

249 citations

Journal Article•10.1021/JE9700582•
Critical Evaluation of the Thermodynamic Properties of Aqueous Calcium Chloride. 1. Osmotic and Activity Coefficients of 0−10.77 mol·kg-1 Aqueous Calcium Chloride Solutions at 298.15 K and Correlation with Extended Pitzer Ion-Interaction Models

[...]

Joseph A. Rard1, Simon L. Clegg2•
Lawrence Livermore National Laboratory1, University of East Anglia2
08 Sep 1997-Journal of Chemical & Engineering Data
TL;DR: In this paper, isopiestic vapor pressure measurements were performed at 298.15 K for CaCl2(aq) solutions at 66 molalities from (4.3235 to 10.253) mol·kg-1, with emphasis given to the accurate characterization of the osmotic coefficients near and above saturation.
Abstract: Isopiestic vapor-pressure measurements were performed at 298.15 K for CaCl2(aq) solutions at 66 molalities from (4.3235 to 10.253) mol·kg-1, using H2SO4(aq) as the reference standard, with emphasis given to the accurate characterization of the osmotic coefficients near and above saturation. Published isopiestic molalities, direct vapor pressures, and emf results for CaCl2(aq) have been critically reevaluated and recalculated in an internally consistent manner. This critically-assessed database was used to evaluate the parameters of Pitzer's equations and various extended forms at 298.15 K and 0.1 MPa. Neither the standard equations nor empirically extended versions were able to represent the thermodynamic results over more than part of the molality range without large cyclic systematic deviations. It was possible, however, to obtain essentially quantitative agreement between experiment and model over the full molality range if (1) the presence of CaCl+(aq) ion pairs was included explicitly and (2) higher-...

133 citations

Journal Article•10.1007/S004100050279•
H2O activity in concentrated KCl and KCl-NaCl solutions at high temperatures and pressures measured by the brucite-periclase equilibrium

[...]

L. Y. Aranovich1, Robert C. Newton1•
University of Chicago1
29 Apr 1997-Contributions to Mineralogy and Petrology
TL;DR: In this paper, H2O activities in supercritical fluids in the system KCl-H2O-(MgO) were measured at pressures of 1, 2, 4, 7, 10 and 15 kbar by numerous reversals of vapor compositions in equilibrium with brucite and periclase.
Abstract: H2O activities in supercritical fluids in the system KCl-H2O-(MgO) were measured at pressures of 1, 2, 4, 7, 10 and 15 kbar by numerous reversals of vapor compositions in equilibrium with brucite and periclase. Measurements spanned the range 550–900 °C. A change of state of solute KCl occurs as pressures increase above 2 kbar, by which H2O activity becomes very low and, at pressures of 4 kbar and above, nearly coincident with the square of the mole fraction (xH2O). The effect undoubtedly results primarily from ionic dissociation as H2O density (ρH2O) approaches 1 gm/cm3, and is more pronounced than in the NaCl-H2O system at the same P-T-X conditions. Six values of solute KCl activity were yielded by terminal points of the isobaric brucite-periclase T-xH2O curves where sylvite saturation occurs. The H2O mole fraction of the isobaric invariant assemblage brucite-periclase-sylvite-fluid is near 0.52 at all pressures, and the corresponding temperatures span only 100 °C between 1 and 15 kbar. This remarkable convergence of the isobaric equilibrium curves reflects the great influence of pressure on lowering of both KCl and H2O activities. The H2O and KCl activities can be expressed by the formulas: aH2O = γH2O[xH2O+(1 + (1 + α)xKCl)], and aKCL = γKCl[(1 + α)xKCl/(xH2O +(1 + α)xKCl)](1 + α), where α is a degree of dissociation parameter which increases from zero at the lowest pressures to near one at high pressures and the γ's are activity coefficients based on an empirical regular solution parameter W: ln γi = (1 − xi)2W. Least squares fitting of our H2O and KCl activity data evaluates the parameters: α = exp(4.166 −2.709/ρH2O) − 212.1P/T, and W = (−589.6 − 23.10P) /T, with ρH2O in gm/cm3, P in kbar and T in K. The standard deviation from the measured activities is only ± 0.014. The equations define isobaric liquidus curves, which are in perfect agreement with previous DTA liquidus measurements at 0.5–2 kbar, but which depart progressively from their extrapolation to higher pressures because of the pressure-induced dissociation effect. The great similarity of the NaCl-H2O and KCl-H2O systems suggests that H2O activities in the ternary NaCl-KCl-H2O system can be described with reasonable accuracy by assuming proportionality between the binary systems. This assumption was verified by a few reconnaissance measurements at 10 kbar of the brucite-periclase equilibrium with a Na/(Na + K) ratio of 0.5 and of the saturation temperature for Na/(Na + K) of 0.35 and 0.50. At that pressure the brucite-periclase curves reach a lowest xH2O of 0.45 and a temperature of 587 °C before salt saturation occurs, values considerably lower than in either binary. This double-salt eutectic effect may have a significant application to natural polyionic hypersaline solutions in the deep crust and upper mantle in that higher solute concentrations and very low H2O activities may be realized in complex solutions before salt saturation occurs. Concentrated salt solutions seem, from this standpoint, and also because of high mechanical mobility and alkali-exchanging potential, feasible as metasomatic fluids for a variety of deep-crust and upper mantle processes.

131 citations

Journal Article•10.1021/ES960227N•
Mass Transfer of Polynuclear Aromatic Hydrocarbons from Complex DNAPL Mixtures

[...]

Suparna Mukherji1, Catherine A. Peters1, Walter J. Weber1•
University of Michigan1
30 Jan 1997-Environmental Science & Technology
TL;DR: In this article, the authors evaluated the rates of mass transfer of the individual components of four synthetic dense non-aqueous phase liquid (DNAPL) mixtures into the aqueous phase.
Abstract: Parameters governing the rates of mass transfer of the individual components of four synthetic dense non-aqueous phase liquid (DNAPL) mixtures into the aqueous phase were evaluated. The DNAPL mixtures, composed of toluene and eight polynuclear aromatic hydrocarbons (PAHs), were designed to serve as models for coal tars and creosotes. The reactor employed provided a relatively stable interface between internally mixed but segregated aqueous and DNAPL phases. Two parameters, the aqueous phase concentration at equilibrium and the overall film mass transfer coefficient, were quantified by simulating aqueous concentration profiles with a mass-transfer-limited rate model using a statistical parameter search and data fitting routine. DNAPL phase activity coefficient values for the various compounds derived from equilibrium aqueous phase concentrations were typically within a factor of 2 of Raoult's law prediction of unity; refinement of fugacity ratio estimates for the solid PAHs brought the values even closer t...

106 citations

Journal Article•10.1021/JE960321J•
Isothermal Vapor−Liquid Equilibria Measurements, Excess Molar Enthalpies, and Excess Molar Volumes of Dimethyl Carbonate + Methanol, + Ethanol, and + Propan-1-ol at 313.15 K

[...]

Fabio Comelli, Romolo Francesconi
14 Jul 1997-Journal of Chemical & Engineering Data
TL;DR: In this paper, isothermal vapor−liquid equilibria (VLE), excess molar enthalpies,, and excess Molar volumes,, have been measured for the binary mixtures dimethyl carbonate + methanol, + ethanol, or + propan-1-ol at 313.15 K and at atmospheric pressure.
Abstract: Isothermal vapor−liquid equilibria (VLE), excess molar enthalpies, , and excess molar volumes, , have been measured for the binary mixtures dimethyl carbonate + methanol, + ethanol, or + propan-1-ol at 313.15 K and at atmospheric pressure. The three mixtures exhibit large deviations from ideality, showing an azeotrope at 0.14, 0.42, and 0.78 mole fraction of dimethyl carbonate, respectively. The VLE data were correlated by the Wilson equation and the appropriate parameters are reported. and values have been correlated using the Redlich−Kister equation by the method of least-squares.

69 citations

Journal Article•10.1021/JE960113R•
Measurements of Vapor Pressures of Aqueous Amino Acid Solutions and Determination of Activity Coefficients of Amino Acids

[...]

Hidetoshi Kuramochi1, Hidetaka Noritomi1, and Daisuke Hoshino1, Kunio Nagahama1•
Tokyo Metropolitan University1
12 May 1997-Journal of Chemical & Engineering Data
TL;DR: In this paper, the activity coefficients of the amino acids in water were derived from the activity coefficient of water using the UNIQUAC equation and evaluated by comparison of the values obtained by a conventional virial expansion method and the literature data.
Abstract: Vapor pressures of aqueous solutions of l-amino acids (glycine, l-alanine, l-valine, and l-serine) were measured at various concentrations at 298 K by a differential pressure static method. Activities and activity coefficients of water were determined. The activity coefficients of the amino acids in water were obtained from the activity coefficients of water using the UNIQUAC equation. The obtained activity coefficients of the amino acids were evaluated by comparison of the values obtained by a conventional virial expansion method and the literature data.

65 citations

Journal Article•10.1021/IE960546N•
Modeling Multicomponent Ion Exchange Equilibrium Utilizing Hydrous Crystalline Silicotitanates by a Multiple Interactive Ion Exchange Site Model

[...]

Z. Zheng1, Rayford G. Anthony1, James E. Miller2•
Texas A&M University1, Sandia National Laboratories2
02 Jun 1997-Industrial & Engineering Chemistry Research
TL;DR: An equilibrium multicomponent ion exchange model for the ion exchange of group I metals by TAM-5, a hydrous crystalline silicotitanate, was presented in this paper.
Abstract: An equilibrium multicomponent ion exchange model is presented for the ion exchange of group I metals by TAM-5, a hydrous crystalline silicotitanate. On the basis of the data from ion exchange and structure studies, the solid phase is represented as Na3X instead of the usual form of NaX. By using this solid phase representation, the solid can be considered as an ideal phase. A set of model ion exchange reactions is proposed for ion exchange between H+, Na+, K+, Rb+, and Cs+. The equilibrium constants for these reactions were estimated from experiments with simple ion exchange systems. Bromley's model for activity coefficients of electrolytic solutions was used to account for liquid phase nonideality. Bromley's model parameters for CsOH at high ionic strength and for NO2- and Al(OH)4- were estimated in order to apply the model for complex waste simulants. The equilibrium compositions and distribution coefficients of counterions were calculated for complex simulants typical of DOE wastes by solving the equil...

64 citations

Journal Article•10.1021/JE970059U•
Phase Equilibria of Binary Systems Formed by Hydrocarbons from Petroleum Fractions and the Solvents N-Methylpyrrolidone and N,N-Dimethylformamide. 1. Isobaric Vapor−Liquid Equilibria

[...]

Beatriz Blanco1, and Sagrario Beltrán1, Jose Luis Cabezas1, José Coca2•
University of Burgos1, University of Oviedo2
08 Sep 1997-Journal of Chemical & Engineering Data
TL;DR: In this article, the same authors reported Isobaric vapor−liquid equilibrium data at 101.33 kPa for binary systems formed by N-methylpyrrolidone (NMP) and N,N-dimethylformamide (DMF) with benzene, heptane, hexane, or cyclohexane.
Abstract: Isobaric vapor−liquid equilibrium data at 101.33 kPa are reported for binary systems formed by N-methylpyrrolidone (NMP) and N,N-dimethylformamide (DMF) with benzene, heptane, hexane, or cyclohexane. Data reduction based on the Van Laar, Wilson, NRTL, and UNIQUAC models provides a correlation for the liquid-phase activity coefficients. All the systems, except for the ones formed with benzene, are strongly nonideal, yielding two phases at low temperatures.

57 citations

Journal Article•10.1016/S0304-386X(96)00074-6•
Critical evaluation of thermodynamics of complex formation of metal ions in aqueous solutions III. The system Cu(I,II) −Cl− −e at 298.15 K

[...]

Mingshen Wang1, Yu Zhang1, Mamoun Muhammed1•
Royal Institute of Technology1
01 May 1997-Hydrometallurgy
TL;DR: A survey of the experimental information on the stability constants and the enthalpy changes for the species of the cuprous and cupric chloride complexes, as well as the equilibrium constant of the disproportionation of cuprous ion to cupric ion and crystalline copper were performed in this article.

56 citations

Journal Article•10.1016/S0009-2541(96)00167-2•
Thermodynamic properties of aqueous species and the solubilities of minerals at high pressures and temperatures: the system Al2O3H2OKOH

[...]

Vitalii A. Pokrovskii, Harold C. Helgeson1•
University of California, Berkeley1
15 May 1997-Chemical Geology
TL;DR: In this article, the authors used the Huckel extended-term parameter for aqueous KOH and dissociation constants for KOH0 generated in the present study with the aid of a speciation model which explicitly provides for the formation in solution of triple ion clusters.

54 citations

Journal Article•10.1016/S0378-3812(97)00145-3•
Prediction of vapor pressure for nonaqueous electrolyte solutions using an electrolyte equation of state

[...]

You-Xiang Zuo, Walter Fürst
01 Nov 1997-Fluid Phase Equilibria
TL;DR: In this article, the aqueous equation of state (EOS) developed by Furst and Renon has been extended to nonaqueous electrolyte solutions, and the predicted results are quite satisfactory, the overall average absolute deviation (AAD) for predicted vapor pressure being approximately 1%.
Journal Article•10.1016/S0378-3812(97)00037-X•
A comparison of Huron-Vidal type mixing rules of mixtures of compounds with large size differences, and a new mixing rule

[...]

Hasan Orbey1, Stanley I. Sandler2•
National University of Singapore1, University of Delaware2
31 May 1997-Fluid Phase Equilibria
TL;DR: In this article, a comparison is made of a number of Huron and Vidal-type mixing rules for mixtures of molecules with large differences in size, and a new mixing rule of this class is introduced.
Journal Article•10.1016/S0378-3812(96)03209-8•
Representation of activity coefficients of fundamental biochemicals in water by the UNIFAC model

[...]

Hidetoshi Kuramochi1, Hidetaka Noritomi1, Daisuke Hoshino1, Kunio Nagahama1•
Tokyo Metropolitan University1
15 Apr 1997-Fluid Phase Equilibria
TL;DR: In this article, the assignment of UNIFAC parameters has been examined to represent the activity coefficients of fundamental biochemicals in aqueous solutions containing sugars, imino acids, urea, amino acid salts, inorganic salts, and sugar salts.
Journal Article•10.1006/JCIS.1997.5081•
Nonideal Mixing in Adsorbed Film and Micelle of Ionic-Nonionic Surfactant Mixtures

[...]

Masumi Villeneuve1, Hirotomo Sakamoto1, Hisanobu Minamizawa1, Norihiro Ikeda2, Kinsi Motomura1, Makoto Aratono1 •
Kyushu University1, Fukuoka Women's University2
15 Oct 1997
TL;DR: The activity coefficient and excess Gibbs energy in the adsorbed film and the micelle were defined and then evaluated and found to give useful information on the deviation from ideal mixing and intermolecular interaction in the advertising film and micelle.
Abstract: The surface tension of aqueous solutions of dodecylammonium chloride–octyl methyl sulfoxide (OMS) and dodecyltrimethylammonium bromide–OMS mixtures was measured as a function of the total molality of surfactants and the composition of OMS. The results were analyzed according to our thermodynamic procedure; the phase diagrams of adsorption and micelle formation and the diagram illustrating the composition relation between the micelle and the adsorbed film at the critical micelle concentration were drawn. The activity coefficient and excess Gibbs energy in the adsorbed film and the micelle were defined and then evaluated from the phase diagrams. They were found to give useful information on the deviation from ideal mixing and intermolecular interaction in the adsorbed film and micelle.
Journal Article•10.1021/JE9700535•
Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 6. Results for Systems Exhibiting Gas−Liquid Interface Adsorption with 1-Octanol

[...]

Detlef Gruber1, Diana Langenheim1, Jürgen Gmehling1, Warren Moollan2•
University of Oldenburg1, University of Natal2
08 Sep 1997-Journal of Chemical & Engineering Data
TL;DR: In this article, the activity coefficients at infinite dilution for various solutes (alkanes, cycloalkane, alcohols, aromatic hydrocarbons, xylenes and alkenes) in the solvent 1-octanol were measured at four temperatures, (293.44, 303.45, 313.55, and 323.43) K, with the help of gas−liquid chromatography.
Abstract: Activity coefficients at infinite dilution provide a useful tool for solvent selection in extractive distillation or extraction processes. In this work activity coefficients at infinite dilution for various solutes (alkanes, cycloalkanes, alcohols, aromatic hydrocarbons, xylenes and alkenes) in the solvent 1-octanol were measured at four temperatures, (293.44, 303.45, 313.55, and 323.43) K, with the help of gas−liquid chromatography. The adsorption at the gas−liquid interface between the solutes and the solvent was examined by varying the solvent liquid loading in the columns. Corrected retention values taking adsorption effects into account are determined and are used to calculate the activity coefficients at infinite dilution. These values compare well with various activity coefficients taken from the literature using different techniques and the predicted values using the modified UNIFAC (Dortmund) method. An important application of the present data can be seen in the use of 1-octanol as a solvent for...
Journal Article•10.1016/S0378-3812(96)03234-7•
Prediction of the solubility and gas-liquid equilibria for gas-water and light hydrocarbonwater systems at high temperatures and pressures with a group contribution equation of state

[...]

Jiding Li1, Isabelle Vanderbeken2, Suyu Ye2, Hervé Carrier2, P. Xans2 •
Tsinghua University1, University of Pau and Pays de l'Adour2
15 May 1997-Fluid Phase Equilibria
TL;DR: In this paper, a group contribution equation of state has been proposed to predict solubility and gas-liquid equilibria for seven gas-water, and thirty-nine light hydrocarbon, data sets in large temperature and pressure ranges (278-637 K, 1-1972 bar).
Journal Article•10.1021/JS9602148•
Analysis of the Solubilization of Steroids by Bile Salt Micelles

[...]

Xiaohong Cai1, David J.W. Grant1, Timothy S. Wiedmann1•
University of Minnesota1
01 Mar 1997-Journal of Pharmaceutical Sciences
TL;DR: The similarity of the relationship between the activity coefficient and the number of hydroxyl groups in the aqueous and micellar solutions indicates the importance of polar interactions for solubilization.
Journal Article•10.1016/S0378-3812(96)03148-2•
Double azeotropy in binary mixtures of NH3 and CHF2CF3

[...]

C.-P. Chai Kao1, Michael E. Paulaitis1, A. Yokozeki1•
University of Delaware1
15 Jan 1997-Fluid Phase Equilibria
TL;DR: In this article, a modified form of the Peng-Robinson equation of state was used to calculate molar volumes and the fugacities of each component in the two phases.
Journal Article•10.1271/BBB.61.1831•
Dielectric Relaxation of Aqueous Solution with Low-molecular-weight Nonelectrolytes and Its Relationship with Solution Structure.

[...]

Akiko Saito1, Osato Miyawaki1, Kozo Nakamura1•
University of Tokyo1
23 Nov 1997-Bioscience, Biotechnology, and Biochemistry
TL;DR: The relaxation time shift of water molecules through the existence of solute was correlated well to the first virial coefficient of the activity coefficient of water suggesting the close relationship between dielectric relaxation time and aqueous solution structure.
Abstract: Dielectric relaxation of water molecules was measured in the frequency range from 0.2 to 20 GHz for aqueous solutions of urea, formamide, alcohols, and saccharides. The relaxation behavior was described well by the Debye equation with a single relaxation process in most cases. The static permittivity of solution and relaxation time of water in solution changed linearly with solute concentration. The relaxation time shift of water molecules through the existence of solute was correlated well to the first virial coefficient of the activity coefficient of water suggesting the close relationship between dielectric relaxation time and aqueous solution structure.
Journal Article•10.1016/S0378-3812(96)03129-9•
Thermodynamic properties of water + normal alcohols and vapor-liquid equilibria for binary systems of methanol or 2-propanol with water

[...]

B. Khalfaoui1, Abdessalem H. Meniai, Rafael Borja2•
University of Manchester1, Spanish National Research Council2
15 Jan 1997-Fluid Phase Equilibria
TL;DR: In this article, experiments were carried out to determine densities and refractive indices of binary and ternary mixtures of water with normal alcohols (methanol and n-butanol) at 293.15 K.
Journal Article•10.1016/S0378-3812(97)00054-X•
Isobaric vapor-liquid equilibria of the methanol, methyl acetate and methyl acrylate system at atmospheric pressure

[...]

Chein-Hsiun Tu1, Yuh-Shen Wu, Tzu-Ling Liu1•
Providence College1
15 Jul 1997-Fluid Phase Equilibria
TL;DR: In this article, the experimental VLE data were reduced and binary parameters for four activity coefficient models, such as Margules, Wilson, NRTL and UNIQUAC, were fitted.
Journal Article•10.1016/S0016-7037(97)00070-7•
Calculation of the standard partial molal thermodynamic properties of KCl0 and activity coefficients of aqueous KCl at temperatures and pressures to 1000°C and 5 kbar

[...]

Vitalii A. Pokrovskii, Harold C. Helgeson1•
University of California, Berkeley1
01 Jun 1997-Geochimica et Cosmochimica Acta
TL;DR: In this article, the Huckel and Setchenow (1892) equations of state were used to regress the experimental activity coefficient and dissociation constant data reported in the literature.
Journal Article•10.1007/BF02767784•
Activity and osmotic coefficients from the EMF of liquid membrane cells. VI-ZnSO4, MgSO4, CaSO4, and SrSO4 in water at 25‡C

[...]

Francesco Malatesta1, Roberto Zamboni1•
University of Pisa1
01 Aug 1997-Journal of Solution Chemistry
TL;DR: In this paper, the activity coefficients of ZnSO4, MgSO 4, CaSO4 and SrSO4 are measured by means of cells with ion-exchange liquid membranes similar to those described in the previous papers of this series.
Abstract: The activity coefficients of ZnSO4, MgSO4, CaSO4, and SrSO4 are measured by means of cells with ion-exchange liquid membranes similar to those described in the previous papers of this series. Negative deviations from the limiting law are observed in the dilute region. These deviations are, for ZnSO4, appreciably more important than recent literature has indicated, and the corresponding activity coefficients need to be corrected by about 12%. Pitzer’s theory best-fit coefficients have accordingly been recalculated. The osmotic coefficients are also derived. Accessory information on the hydration state for zinc, magnesium, and sulfate ions, is presented.
Journal Article•10.1016/S0921-5093(97)00593-5•
Activity of aluminum in molten Ti–Al alloys

[...]

Masafumi Maeda1, Tomoyoshi Kiwake1, Katsuhiko Shibuya1, Takashi Ikeda1•
University of Tokyo1
01 Dec 1997-Materials Science and Engineering A-structural Materials Properties Microstructure and Processing
TL;DR: In this article, the free evaporation method was used to measure the activity of aluminum in molten Ti-Al alloy and the Gibbs-Knudsen equation was applied to calculate the vapor pressure of the element.
Abstract: The activity of aluminum in molten Ti–Al alloy was measured by `free evaporation method'. The specimen was melted and held at constant temperature in an electron beam vacuum furnace. The weight change was measured and converted to the rate of evaporation of constant composition. The Hertz–Knudsen equation was then applied to calculate the vapor pressure of the element, and the activity was obtained by comparing that with the pressure of the pure substance. The activity coefficient at mole fractions of aluminum less than 0.1 is about 0.03 and that for over 0.2 was about 0.1. The activity of titanium was also calculated by integration of the Gibbs–Duhem equation for a binary mixture based on the activity of aluminum.
Journal Article•10.1016/S0378-3812(97)00188-X•
Thermodynamic representation of the solubility for potassium dihydrogen phosphate (KDP) + water + alcohols systems

[...]

Paulo A. Barata1, Maria L. Serrano1•
Technical University of Lisbon1
01 Dec 1997-Fluid Phase Equilibria
TL;DR: In this paper, a visual polythermal method was used to determine the ternary solubility of potassium dihydrogen phosphate (KDP) in water and in aqueous solutions of ethanol, 1-propanol, and 2-Propanol.
FREZCHEM2 : a chemical thermodynamic model for electrolyte solutions at subzero temperatures

[...]

Mikhail V. Mironenko, Steven A. Grant, Giles M. Marion, Ronald E. Farren
1 Oct 1997
TL;DR: In this article, a Fortran version of a chemical thermodynamic model for aqueous electrolyte solutions at subzero temperatures, FREZCHEM2, which is a further development of the FrezCHEM model, is presented.
Abstract: : This report documents a Fortran version of a chemical thermodynamic model for aqueous electrolyte solutions at subzero temperatures, FREZCHEM2, which is a further development of the FREZCHEM model. The model uses thermodynamic data of Spencer-Moller- Weare that permit the calculation of chemical equilibria in the Na-K-Ca-Mg-Cl-S04-H2O system between -60 and 25 deg. C at atmospheric pressure. It applies the Gibbs energy minimization method for chemical equilibrium computation combined with Pitzer equations for activity coefficients and water activity calculation. phases.
Journal Article•10.1021/JP9721863•
A calorimetric study of the influence of electrolyte on the micellisation of phenothiazine drugs in aqueous solution

[...]

David Attwood1, Elisabeth Boitard2, J.P. Dubes2, H. Tachoire2•
University of Manchester1, University of Provence2
01 Nov 1997-Journal of Physical Chemistry B
TL;DR: In this article, a mass action model of association based on the Guggenheim equations for the activity coefficients for mixed electrolytes was used to determine the apparent molar enthalpies of phenothiazine drugs.
Abstract: Apparent molar enthalpies have been determined as a function of concentration by heat conduction calorimetry for aqueous solutions of the phenothiazine drugs chlorpromazine hydrochloride, promethazine hydrochloride, and promazine hydrochloride in the presence of added electrolyte (0.025−0.10 mol dm-3 NaCl). The concentration dependence of the apparent molar enthalpy could be quantitatively described using a mass action model of association based on the Guggenheim equations for the activity coefficients for mixed electrolytes. Derived values of the monomer−counterion interaction coefficient became increasingly negative with increase of salt concentration, suggesting that electrolyte addition promoted association at concentrations below the critical micelle concentration (cmc). Calculations of the fraction of each drug in the form of micelles as a function of concentration further confirmed the tendency for premicellar association. Significant differences in properties were observed between promethazine and...
Journal Article•10.1016/S0304-386X(96)00072-2•
Critical evaluation of thermodynamics of complex formation of metal ions in aqueous solutions I. A description of evaluation methods

[...]

Mingsheng Wang1, Yu Zhang1, Mamoun Muhammed1•
Royal Institute of Technology1
01 May 1997-Hydrometallurgy
TL;DR: In this paper, it has been shown that the SIT model is the most suitable method for evaluating the values of log K and ΔrH° at infinite dilution and for reproducing the dependence of log k and Δ rH on the ionic medium and concentration.
Journal Article•10.1007/BF02706075•
Vapor-liquid equilibria for the binary monoethanolamine+ water and monoethanolamine+ethanol systems

[...]

Seong-Beom Park1, Hun Lee1•
KAIST1
01 Mar 1997-Korean Journal of Chemical Engineering
TL;DR: The experimental data were verified to be thermodynamically consistent and showed a good agreement with the calculated values as mentioned in this paper, and the results were checked for thermodynamic consistency by the point test method.
Abstract: Isobaric vapor-liquid equilibrium data for monocthanolamine (MEA)+water and monoethanolamine (MEA)+ ethanol were measured in an equilibrium cell circulating both the vapor and liquid phases. The measurements of the boiling temperatures and corresponding equilibrium compositions for two binary mixtures were carried out at the atmospheric pressure. The results were checked for thermodynamic consistency by the point test method. The activity coefficients for nonideality of the liquid phase were calculated by using the Wilson, NRTL, and UNIQUAC equations. The fugacity coefficients for nonideality of the vapor phase were calculated from the virial equation of state with the second virial coefficient. The experimental data were verified to be thermodynamically consistent and showed a good agreement with the calculated values.
Journal Article•10.1007/BF02768052•
Interactions of DL-serine and L-serine with NaCl and KCl in aqueous solutions

[...]

Mohammad K. Khoshkbarchi1, Ana M. Soto-Campos1, Ana M. Soto-Campos2, Juan H. Vera1•
McGill University1, University of Santiago de Compostela2
01 Oct 1997-Journal of Solution Chemistry
TL;DR: In this paper, the authors examined the effect of the nature of the cation of the electrolyte on the activity coefficients of the optical-isomers of serine in aqueous solutions for molality up to 0.4 and molality of electrolyte up to 1.
Abstract: The activity coefficients at 25‡C of DL-serine and L-serine in aqueous solutions of NaCl and KC1 were measured. This study examines the effect of the nature of the cation of the electrolyte on the activity coefficients of the optical-isomers of serine in aqueous solutions for molality of serine up to 0.4 and molality of electrolyte up to 1. An electrochemical cell with two ion-selective electrodes, a cation, and an anion ion selective electrode,vs. a double-junction reference electrode was used to measure the activity coefficients of the electrolyte and the results were converted to the activity coefficients of serine in the aqueous electrolyte solution. The comparison of the results obtained for DL- and L-serine indicates that the two optical isomers have identical interactions with electrolytes in aqueous solutions and that for this amino acid the effect of the cation of the electrolyte is not significant. Comparison of these results with previous measurements for DL-alanine in aqueous solutions of the same electrolytes show the notable effect of the backbone of the amino acid.
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