The Solubility, Activity Coefficients and Solubility Product of Manganese(II) Iodate1a

1951 ◽  
Vol 73 (10) ◽  
pp. 4853-4855 ◽  
Author(s):  
Anson Mack Hayes ◽  
Don S. Martin
1960 ◽  
Vol 38 (1) ◽  
pp. 161-170
Author(s):  
Y. Iyengar

Theoretical equations have been derived for calculating heats of solutions of an electrolyte in its saturated system comprising one or more electrolytes. These expressions involve the application of "Harned's rule" concerning activity coefficients in mixed electrolytic solutions to an extension of van't Hoff's equation dealing with the temperature coefficient of solubility product in non-ideal systems. The commonly occurring case of mixed electrolytic pairs has been considered in detail. Application of theoretical equations to calculate the heats of solutions KCl, NaCl, and KNO3 in the saturated systems KCl–NaCl–H2O and KCl–KNO3–H2O is briefly discussed.


2017 ◽  
Vol 51 (4) ◽  
pp. 315-328
Author(s):  
Arturo Mendoza-Flores ◽  
Mario Villalobos ◽  
Teresa Pi-Puig ◽  
Nadia Valentina Martínez-Villegas

1994 ◽  
Vol 59 (8) ◽  
pp. 1738-1744
Author(s):  
Vladislav Holba

The solubilities of tetraalkylammonium dianilinetetraisothiocyanatochromates(III) (alkyl = methyl, ethyl, 1-propyl, and 1-butyl) in water, water - methanol, water - tert-butyl alcohol and water - acetonitrile solutions were measured at 25 °C. The results were used to evaluate the activity coefficients and Gibbs energies of transfer of the saturating salts from water to the mixed systems. The Gibbs energies of transfer of the [Cr(C6H5NH2)2(NCS)4]- ion were obtained by means of known ionic transfer functions for the tetraalkylammonium ions based on the TATB assumption.


1989 ◽  
Vol 54 (11) ◽  
pp. 2840-2847 ◽  
Author(s):  
Ivona Malijevská ◽  
Alena Maštalková ◽  
Marie Sýsová

Isobaric equilibrium data (P = 101.3 kPa) for the system cyclohexane-acetic acid-propionic acid have been measured by two different analytical techniques. Activity coefficients calculated by simultaneous solving of equations for the chemical and phase equilibria were subjected to a consistency test based on inaccuracies determined from the error propagation law, and were correlated by Wilson’s equation. The activity coefficients measured were compared with those calculated from binary vapour-liquid equilibrium data and with values predicted by the UNIFAC method.


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