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  • Inorganic Chemistry  (1)
  • magnesium  (1)
  • methanol tetramer  (1)
  • 1
    ISSN: 1572-8927
    Keywords: Phase equilibrium: solubility ; carbonates ; magnesium ; eitelite ; Pitzer model ; carbonic acid ; carbonato complex formation
    Source: Springer Online Journal Archives 1860-2000
    Topics: Chemistry and Pharmacology
    Notes: Abstract The stoichiometric solubility constant of eitelite (NaMg 0.5 CO 3 +2H+ ⇄ Na++0.5Mg 2+ +CO 2 (g)+H 2 O, log*K pso I =14.67±0.03 was determined at I=3 m (mol kg−1) (NaClO 4 ) and 25°C. The stability of magnesium (hydrogen-)carbonato complexes in this ionic medium was explicitely taken into account. Consequently, trace activity coefficients of free ionic species, calculated from the Pitzer model with ion-interaction parameters from the literature, were sufficient for an evaluation of the thermodynamic solubility constants and Gibbs energies of formation for eitelite (−1039.88±0.60), magnesite (−1033.60±0.40), hydromagnesite (−1174.30±0.50), nesquehonite (−1724.67±0.40), and brucite (−835.90±0.80 kJ-mol −1 ). The increasing solubilities of nesquehonite and eitelite at higher sodium carbonate molalities were explained by invoking a magnesium dicarbonato complex (Mg2++2CO 3 2− ⇄ Mg(CO3) 2 2− , log βz = 3.90 ± 0.08). A set of ion-interaction parameters was obtained from solubility and dissociation constants for carbonic acid in 1 to 3.5 m NaClO 4 media $$(\theta _{HCO_3^ - ,ClO_4^ - } = 0.081, \theta _{CO_3^{2 - } ,ClO_4^ - } = 0.071, \psi _{{\rm N}a^ + , HCO_3^ - , ClO_4^ - } = - 0.019,\psi _{{\rm N}a^ + , CO_3^{2 - } , ClO_4^ - } = - 0.006,\lambda _{ClO_4^ - ,CO_2 } = - 0.076)$$ which reproduce these constants to 0.02 units in log K. The following Pitzer parameters are consistent with the previously studied formation of magnesium (hydrogen-)carbonato complexes in 3m NaClO 4 $$(\psi _{Mg^{2 + } , HCO_3^ - , ClO_4^ - } = - 0.36, \lambda _{ClO_4^ - ,MgCO_3 } = 0.081)$$ . The model and Gibbs functions of solid phases derived here reproduce original solubility data (−log [H+], [Mg 2+ ] tot ) measured in perchlorate medium within experimental uncertainty.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Journal of solution chemistry 29 (2000), S. 505-520 
    ISSN: 1572-8927
    Keywords: Cyclohexane ; methanol ; thermodynamic modeling ; virial coefficient formalism ; methanol tetramer ; phase diagram ; high temperature
    Source: Springer Online Journal Archives 1860-2000
    Topics: Chemistry and Pharmacology
    Notes: Abstract The phase diagram of cyclohexane-methanol was thermodynamically modeledin the range of 150 ≤ T/K ≤ 360 and at a pressure of 1 bar on the basis ofavailable experimental data. The Gibbs energy functions of four pure solid andtwo mixture phases were taken into consideration. The liquid phase was describedby a model based on mole fraction statistics and the simplified assumption ofmethanol tetramers mixed with cyclohexane monomers. The gas phase was treatedas a nonideal mixture with a Gibbs energy modeled on the basis of the virialcoefficient formalism considering only monomers. The Gibbs energies of the twosolid modifications of pure methanol, as well as pure cyclohexane, were fixedusing literature data. The pressure dependence of the Gibbs energies of the liquidand solid phases were neglected. The complete T-x phase diagram includinggas/liquid equilibria as well as p-x phase diagrams in the range of 20 and 55°C werecalculated. Experimental and calculated data were found to agree reasonably well.
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  • 3
    Electronic Resource
    Electronic Resource
    Weinheim : Wiley-Blackwell
    Zeitschrift für anorganische Chemie 584 (1990), S. 185-193 
    ISSN: 0044-2313
    Keywords: Chemistry ; Inorganic Chemistry
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology
    Description / Table of Contents: Phasengleichgewichte zwischen Festkörpern und wäßrigen Lösungen. IV. Berechnung von PhasendiagrammenDie thermodynamischen Grundlagen von konventionellen (T-x, P-T) Phasen- und Löslichkeitsdiagrammen (log ΣK-x) werden von einem einheitlichen Gesichtspunkt aus behandelt; letztere bilden Phasengleichgewichte zwischen Festkörper und Lösung in wäßrigen Medien ab. Es wird gezeigt, daß man aus Löslichkeitsmessungen erhaltene thermodynamische Größen zur Konstruktion von konventionellen Phasendiagrammen verwenden kann. Das Einstoffsystem Calcit-Aragonit und das Zweistoffsystem Aragonit-Strontianit, bei dem Löslichkeitsdaten im ganzen Bereich der Zusammensetzung vorhanden sind, wurden als Beispiele ausgewählt. Im binären Fall spielt die auch experimentell festgestellte Invarianz der Zusammensetzung fester Mischphasen, die sich im metastabilen Gleichgewicht mit der Lösung befinden, eine entscheidene Rolle für die Formulierung der maßgeblichen thermodynamischen Beziehungen.
    Notes: The thermodynamic principles of conventional (T-x, P-T) phase diagrams and solubility (log ΣK-x) diagrams depicting solid-solute phase equilibria in aqueous solution are derived from a unifying point of view. It is shown that thermodynamic quantities necessary for the construction of conventional phase diagrams can be obtained from solubility measurements. The unary system calcite-aragonite and the binary system aragonite-strontianite, where solubility data are available over the whole compositional range, have been selected as examples. In the latter case, the constraint of constant composition of the solid phase leading to a metastable equilibrium with the respective solute species is an essential point in the thermodynamic derivation and was observed experimentally as well.
    Additional Material: 4 Ill.
    Type of Medium: Electronic Resource
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