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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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10.4 Acid-base equilibria in ionic solvents 633<br />

NaI + 1/ 2O = 1/ 2Na O + 1/ 2I<br />

[10.4.51]<br />

2 2 2 2<br />

are 32.8±2 and 13.9±1 kJ/mole for solid NaI and 30.6±2 and 9.3±2 kJ/mole for liquid one.<br />

These values suggest that NaI has a greater tendency to oxidation than to hydrolysis. This<br />

conclusions cannot be adopted without stipulation, because it is based on values ΔH and not<br />

ΔG, although only the latter values determine the direction <strong>of</strong> a reversible reactions at constant<br />

p and T.<br />

A simple but unquestionable method has been used to investigate high-temperature<br />

hydrolysis <strong>of</strong> molten KCl-NaCl. 104 A mixture <strong>of</strong> HCl and H 2O obtained by passing an inert<br />

gas through aqueous solutions at a definite concentration was passed into the melt. Measurements<br />

<strong>of</strong> the equilibrium O 2- concentration by potentiometric method allowed to calculate<br />

the equilibrium constants <strong>of</strong> [10.4.13] as pK=55.3×10 3 T -1 -40.2. At 1000, pK=15.1, it<br />

means that equilibrium [10.4.13] in molten KCl-NaCl is displaced to the left.<br />

A similar method has been used to study the hydrolysis <strong>of</strong> the eutectic KCl-LiCl at<br />

500 o C (pK=9.77±0.4). 105 The hydrolysis <strong>of</strong> the chloride melt is thermodynamically unfavorable<br />

and is completely suppressed in the presence <strong>of</strong> bases (even at a concentration <strong>of</strong><br />

~10 -3 mole/kg).<br />

The potentiometric cells:<br />

( H O + H ) Au NMeOH + ( 1−N)<br />

MeX MeX C( X )<br />

| || | [10.4.52]<br />

2 2 2<br />

were used to investigate the hydrolysis <strong>of</strong> individual alkaline halide melts (with the exception<br />

<strong>of</strong> the lithium salts). 106<br />

The e.m.f. <strong>of</strong> cell [10.4.52] is related to the concentration <strong>of</strong> the reactants by the expression:<br />

0<br />

E = E +<br />

RT<br />

F<br />

P P<br />

ln<br />

P<br />

12 / 12 /<br />

H2 X2<br />

HO 2<br />

a<br />

MeOH<br />

[10.4.53]<br />

1/ 2 1/ 2<br />

where PH and P<br />

2 X are partial pressures <strong>of</strong> hydrogen and halogen over the melt, respec-<br />

2<br />

tively.<br />

The logarithms <strong>of</strong> the equilibrium constants<br />

F<br />

lnK ln<br />

RT E<br />

G P P<br />

= − +<br />

RT P<br />

/ /<br />

Δ HX H X<br />

0 12 12<br />

2 2<br />

HO 2<br />

a<br />

MeOH<br />

[10.4.54]<br />

are negative for all the melts studied, which indicates that the hydrolysis <strong>of</strong> alkali metal halide<br />

melts is thermodynamically unfavorable. The trend towards hydrolysis <strong>of</strong> melts <strong>of</strong> individual<br />

alkaline halides diminishes with the increase in the radii <strong>of</strong> both cation and anion.<br />

According to the results <strong>of</strong> Smirnov et al. 106 the solutions <strong>of</strong> alkali metal hydroxides in the<br />

corresponding individual halides are close to ideality.<br />

10.4.5.2 The processes <strong>of</strong> removal <strong>of</strong> oxide admixtures from melts<br />

The studies <strong>of</strong> the elimination <strong>of</strong> oxygen containing impurities from ionic melts are <strong>of</strong> an<br />

applied character and are performed in melts having industrial applications. Various

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