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chemical thermodynamics of neptunium and plutonium - U.S. ...

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32 2. St<strong>and</strong>ards, Conventions, <strong>and</strong> Contents <strong>of</strong> the Tablesthe data are also stored in the data base.The following thermodynamic parameters, valid at the reference temperature <strong>of</strong>298.15 K <strong>and</strong> at the st<strong>and</strong>ard pressure <strong>of</strong> 1 bar, are stored in the data base: f G ◦ m the st<strong>and</strong>ard molar Gibbs energy <strong>of</strong> formation from (kJ · mol −1 )the elements in their reference state f Hm◦ the st<strong>and</strong>ard molar enthalpy <strong>of</strong> formation from the elements(kJ · mol −1 )in their reference stateSm ◦ the st<strong>and</strong>ard molar entropy (J · K −1 · mol −1 )Cp,m ◦ the st<strong>and</strong>ard molar heat capacity (J · K −1 · mol −1 )<strong>and</strong> C◦ p,mFor aqueous neutral species <strong>and</strong> ions, the values <strong>of</strong> f G ◦ m , fHm ◦ , S◦ mcorrespond to the st<strong>and</strong>ard partial molar quantities, <strong>and</strong> for individual aqueous ions theyare relative quantities, defined with respect to the aqueous hydrogen ion, according tothe convention [89COX/WAG] that f Hm ◦ (H+ , aq,T ) = 0, <strong>and</strong> that Sm ◦ (H+ , aq,T ) =0. Furthermore, for an ionised solute B containing any number <strong>of</strong> different cations <strong>and</strong>anions: f H ◦ m (B ±, aq) = ∑ +ν + f H ◦ m (cation, aq) + ∑ −ν − f Hm ◦ (anion, aq)S ◦ m (B ±, aq) = ∑ +ν + S ◦ m (cation, aq) + ∑ −ν − Sm ◦ (anion, aq).As the thermodynamic parameters vary as a function <strong>of</strong> temperature, provision is madefor including the compilation <strong>of</strong> the coefficients <strong>of</strong> empirical temperature functions forthese data, as well as the temperature ranges over which they are valid. In many casesthe thermodynamic data measured or calculated at several temperatures were publishedfor a particular species, rather than the deduced temperature functions. In these cases,a non-linear regression method is used in this review to obtain the most significantcoefficients <strong>of</strong> the following empirical function:F(T ) = a + b × T + c × T 2 + d × T −1 + e × T −2 + f × ln T + g × T ln T+ h × √ T + i √T+ j × T 3 + k × T −3 . (2.52)Most temperature variations can be described with three or four parameters, a, b <strong>and</strong>e being the ones most frequently used. In the present review, only Cp,m ◦ (T ), i.e., thethermal functions <strong>of</strong> the heat capacities <strong>of</strong> individual species, are considered <strong>and</strong> storedin the data base. They refer to the relationC ◦ p,m (T ) = a + b × T + c × T 2 + d × T −1 + e × T −2<strong>and</strong> are listed in Tables 3.3 <strong>and</strong> 4.3.The pressure dependence <strong>of</strong> thermodynamic data has not been the subject<strong>of</strong> critical analysis in the present compilation. The reader interested in highertemperatures <strong>and</strong> pressures, or the pressure dependency <strong>of</strong> thermodynamic functionsfor geo<strong>chemical</strong> applications, is referred to the specialised literature in this area, e.g.,

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