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

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B.1 2BThe specific ion interaction equations<br />

437<br />

• Assumption 1: The activity coefficient γ j <strong>of</strong> an ion j <strong>of</strong> charge z j in the solution<br />

<strong>of</strong> ionic strength I m may be described by Eq. (B.1):<br />

D is the Debye-Hückel term:<br />

2<br />

log<br />

10<br />

γ<br />

j<br />

= zj D ε( j, k, Im)<br />

mk<br />

k<br />

A Im<br />

D =<br />

1 + Ba I<br />

− + ∑ (B.1)<br />

j<br />

m<br />

(B.2)<br />

A and B are constants which are temperature and pressure dependent, a j is an ion size<br />

parameter (“distance <strong>of</strong> closest approach”) for the hydrated ion j, and I m is the molal<br />

ionic strength:<br />

I<br />

= 1<br />

∑ mz 2<br />

2<br />

m i i<br />

i<br />

The Debye-Hückel limiting slope, A, has a value <strong>of</strong> (0.509 ± 0.001)<br />

1 1<br />

2 2<br />

kg ·mol − at 298.15 K and 1 bar, (cf. Section B.1.2). The term Ba j in the denominator<br />

<strong>of</strong> Eq. (B.2) (where a j is an “effective” ion size parameter and B is a constant determined<br />

by the temperature and the physical properties <strong>of</strong> water) has been assigned an<br />

1 1<br />

2 2<br />

empirical value <strong>of</strong> 1.5 kg ·mol −<br />

(Eq. (B.2a)). The value 1.5 was proposed by<br />

Scatchard [1976SCA] to minimise the ionic strength dependence <strong>of</strong> ε ( jk , ) for a number<br />

<strong>of</strong> electrolytes, and it was found to be particularly appropriate between I m = 0.5 and<br />

3.5 m. A constant value <strong>of</strong> Ba j for all species simplifies modelling <strong>of</strong> both binary and<br />

multicomponent aqueous electrolyte systems, and makes it easier to give a consistent<br />

description <strong>of</strong> mean activity coefficient both in binary and multicomponent solutions<br />

([1959ROB/STO], pp.435-441). Thus,<br />

1<br />

AI 2<br />

m<br />

D = (B.2a)<br />

1<br />

1 + 1.5I<br />

2<br />

m<br />

It should be mentioned that some authors have proposed different values for<br />

Ba j ranging from Ba j = 1.0 [1935GUG] to Ba j = 1.6 [1962VAS]. However, the parameter<br />

Ba j is empirical and as such is correlated to the value <strong>of</strong> ε ( jkI , , m<br />

). Hence, this variety<br />

<strong>of</strong> values for Ba j does not represent an uncertainty range, but rather indicates that<br />

several different sets <strong>of</strong> Ba j and ε ( jkI , , m<br />

) may describe equally well the experimental<br />

mean activity coefficients <strong>of</strong> a given electrolyte. The ion interaction coefficients at<br />

298.15 K listed in Table B-4, Table B-5, Table B-6 and Table B-7 have thus to be used<br />

1 1<br />

2 2<br />

with Ba j = 1.5 kg ·mol − .<br />

The summation in Eq. (B.1) extends over all ions k present in solution. Their<br />

molality is denoted by m k , and the specific ion interaction parameters, ε ( jkI , , m<br />

), in<br />

general depend only slightly on the ionic strength. The concentrations <strong>of</strong> the ions <strong>of</strong> the<br />

ionic medium are <strong>of</strong>ten very much larger than those <strong>of</strong> the reacting species. Hence, the<br />

ionic medium ions will make the main contribution to the value <strong>of</strong> log 10 γ j for the reacting<br />

ions. This fact <strong>of</strong>ten makes it possible to simplify the summation ∑ ε( jkI , , ) m ,<br />

k<br />

m<br />

k<br />

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

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