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Chemical Thermodynamics of Tin - Volume 12 - OECD Nuclear ...

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366<br />

A Discussion <strong>of</strong> selected references<br />

[1979VAS/GLA]<br />

Redox potentials for Sn 4+ /Sn 2+ in perchloric acid solutions containing SnCl 2 and SnCl 4<br />

were determined at 25 °C and ionic strength 2 − 4 M HClO 4 , using the cell:<br />

Pt, H 2 | HClO 4 SnCl 2 , SnCl 4 , HClO 4 | Hg, Pt.<br />

After 3 to 3.5 h electrode potentials were stable shifting less than 0.02 mV per<br />

hour, thus indicating equilibration. Concentration <strong>of</strong> Sn 2+ was determined<br />

iodometrically after measuring electrode potentials.<br />

Equilibrium concentrations <strong>of</strong> Sn 2+ and Sn 4+ were calculated considering<br />

hydrolysis (Sn(OH) 3+ 2<br />

, Sn(OH) + 2 , Sn(OH) + 3 , Sn(OH) 4 ) [1971NAZ/ANT] and chlorido<br />

complex formation (SnCl + , SnCl 2 , SnCl − 3 ) using constants from literature including<br />

work <strong>of</strong> their own group.<br />

The standard potential <strong>of</strong> the half-cell Sn 2+ , Sn 4+ | Hg, Pt according to reaction<br />

Sn 4+ + H 2 (g) Sn 2+ + 2 H +<br />

(G)<br />

(A.72)<br />

ο<br />

was found to be E (Sn 4+ /Sn 2+ ) = (0.1522 ± 0.0005) V. The calculated Gibbs energy <strong>of</strong><br />

formation <strong>of</strong> Sn 4+ ο<br />

in aqueous solution is Δ G (Sn 4+ ) = (1.63 ± 0.13) kJ·mol –1 .<br />

f<br />

The results <strong>of</strong> Vasil’ev et al. are flawed by two numerical mistakes.<br />

m<br />

(1) While Eqs. (6), (7) and (8) used in [1979VAS/GLA] for extrapolation to ionic<br />

strength I = 0 are quite correct, – ψ(I) has erroneously been ascribed a negative<br />

value.<br />

(2) In the original Table 2 <strong>of</strong> [1979VAS/GLA] row 13 and 14 <strong>of</strong> column 8 as well<br />

as column 9 should be exchanged.<br />

In addition Vasil’ev et al. conclude from earlier experiments [1977VAS/GLA]<br />

that SnCl 4 and (NH 4 ) 2 SnCl 6 dissociate completely in 0.6 to 2.0 M HClO 4 .<br />

In Table A-42 the experimental data <strong>of</strong> [1979VAS/GLA] are listed. As the SIT<br />

method is based on molality as composition variable these data were transformed by the<br />

following semi-empirical equation:<br />

m = c ⋅ [1 / d + a⋅ c + b⋅ c ]<br />

(A.73)<br />

o 2<br />

B B w − − − −<br />

(ClO4 + Cl ) (ClO4<br />

+ Cl )<br />

o<br />

where at 25 °C c B , d<br />

w<br />

= 0.997045 kg·dm –3 , c − −<br />

(ClO4<br />

+ Cl ) , and a = 0.044672<br />

dm 6·mol –1·kg –1 , b = 0.002291 dm 9·mol –2·kg –1 are the concentration <strong>of</strong> substance B given<br />

in Table A-42, the density <strong>of</strong> pure H 2 O, the total anion concentration, and the empirical<br />

fit parameters when Eq. (A.73) is regressed using ξ(HClO 4 ) = mHClO4/<br />

c HClO4<br />

listed in<br />

Table II-5. In the pertinent case c HClO4<br />

>> c −<br />

Cl and thus the ξ(HClO 4 ) values should be<br />

a reasonable approximation to the real ones.<br />

CHEMICAL THERMODYNAMICS OF TIN, ISBN 978-92-64-99206-1, © <strong>OECD</strong> 20<strong>12</strong>

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