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

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VII.2 Solid tin oxides and hydroxides <strong>12</strong>9<br />

Gurevich et al. [2004GUR/GAV2] and [2004GUR/GAV3] measured the heat<br />

capacity <strong>of</strong> SnO 2 (cass) in the temperature range <strong>of</strong> 13.4 to 336 K using an adiabatic<br />

calorimeter. Two samples <strong>of</strong> tin dioxide with w(SnO 2 ) = 99.906 %(RP) and w(SnO 2 ) =<br />

99.996 %(AA), respectively, were investigated, see Table A-70. They used the Debye-<br />

Einstein-Kieffer equation to fit their experimental data (see Eq. (A.85)). The resulting<br />

data on heat capacity and entropy are displayed in Table VII-5 and compared with a<br />

conventional fitting equation which was conducted as follows.<br />

Table VII-5: Comparison <strong>of</strong> thermodynamic data <strong>of</strong> SnO 2 (tetragonal) at 298.15 K.<br />

[2004GUR/GAV2]<br />

this review<br />

o<br />

C<br />

p, m<br />

/J·K –1·mol –1 55.24 ± 0.03 55.26 ± 0.09<br />

ο<br />

S<br />

m<br />

/J·K –1·mol –1 51.82 ± 0.07 51.77 ± 0.14<br />

[ H ο ( T) − H<br />

ο (0K) ]/kJ·mol –1<br />

8.806 ± 0.005 8.805 ± 0.017<br />

m<br />

m<br />

The first step was to examine up to which temperature the heat capacity <strong>of</strong><br />

SnO 2 (cr) obeys Debye’s T 3 ο<br />

law, see Figure VII-11. In fact the first 17 C p,m<br />

values <strong>of</strong><br />

[1980ZHO/KOS] and [2004GUR/GAV3] are within the experimental uncertainty<br />

proportional to T 3 ο<br />

and at 16 K the heat capacity ( (SnO 2 cr, 16 K) = 0.168<br />

J·K –1·mol C p,m<br />

–1 ) agrees closely with that derived by Gurevich et al. From T 0 = 16 K to<br />

ο<br />

336 K, Cp<br />

,m ( T ) was approximated by Eq. (VII.25) containing 6 adjustable parameters<br />

ο<br />

(a to f ) whose numerical values refer to /J·K –1·mol –1 and T/K, see also Table A-73.<br />

C p,m<br />

ο<br />

ο<br />

[ C (T) – (T 0 )]/J·K –1·mol –1 = a [(T – T 0 )/K]+ b [(T/K) 2 – (T 0 /K) 2 p,m<br />

C p,m<br />

]<br />

+ c [(T/K) –2 – (T 0 /K) –2 ] + d [(T/K) –3 – (T 0 /K) –3 ]<br />

+ e [(T/K) –0.5 – (T 0 /K) –0.5 ] + f [(T/K) –1 – (T 0 /K) –1 ]<br />

(VII.25)<br />

a b c d e f<br />

Eq. (VII.25) 1.7419×10 –1 – 2.1858×10 –4 – 2.9144×10 4 1.1389×10 5 – 1.0659×10 3 4.4830×10 3<br />

ο<br />

The uncertainty <strong>of</strong> C ( ) p,m<br />

T<br />

was estimated by<br />

N<br />

ο ο 2<br />

∑ { Cp,m (obsd) − Cp,m(calc)}<br />

ο 1<br />

,m<br />

=<br />

sC ( p<br />

)<br />

N − 7<br />

= 0.089 J·K –1·mol –1 .<br />

Thermodynamic functions<br />

T<br />

ο<br />

ο<br />

m<br />

= ∫ p,m<br />

0K<br />

S ( T) ( C / T)dT<br />

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

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