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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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9.3 Physical properties <strong>of</strong> mixed solvents 515<br />

<strong>of</strong> permittivity, α ε , <strong>of</strong> the equivolume mixture <strong>of</strong> two chemically non-interacting associated<br />

solvents is carried out using the equation identical in its form to [9.26].<br />

where<br />

( )<br />

Δα = 05 . α − α + α −Δα<br />

[9.27]<br />

1 2 2<br />

ε, V= 05 . ε ε ε ε,<br />

V=<br />

05 .<br />

( )<br />

Δα = 0. 043 α −α/<br />

α<br />

[9.28]<br />

1 2<br />

ε, V= 05 . ε ε ε,<br />

V=<br />

05 .<br />

9.3.1.2 Viscosity<br />

There are a great number <strong>of</strong> equations available in literature intended to describe viscosity<br />

<strong>of</strong> mixtures <strong>of</strong> chemically non-interacting components. All these equations, regardless <strong>of</strong><br />

whether they have been derived theoretically or established empirically, are divided into<br />

two basic groups. The first group includes equations relating mixture viscosity,η, to viscosity<br />

<strong>of</strong> initial components, ηi, and their content in mixture, c, (c in this case is an arbitrary<br />

method <strong>of</strong> concentration expression):<br />

( , , ; , , )<br />

η f η η �η c c � c<br />

[9.29]<br />

= 1 2 i 1 2 i−1<br />

The equations <strong>of</strong> the second group include various constants k 1,k 2, etc., found from<br />

experiment or calculated theoretically<br />

( , , ; , , ; , , )<br />

η f η η �η c c �c k k � [9.30]<br />

= 1 2 i 1 2 i−1<br />

1 2<br />

The accuracy <strong>of</strong> calculation <strong>of</strong> solvents mixture viscosity from [9.30] type <strong>of</strong> equations<br />

is not higher than from equations <strong>of</strong> [9.29] type. We, thus, limit discussion to equations<br />

[9.29].<br />

The comparison <strong>of</strong> equations <strong>of</strong> type [9.29] for binary liquid systems 3 has shown that,<br />

in most cases, viscosity <strong>of</strong> systems with chemically non-interacting components is described<br />

by the exponential function <strong>of</strong> molar-fractional composition<br />

i<br />

xi<br />

=∏ i<br />

η η<br />

1<br />

or for binary solvent:<br />

η= η η<br />

x 1−x<br />

1 2<br />

[9.31]<br />

[9.31a]<br />

where:<br />

xi molar fractions <strong>of</strong> components <strong>of</strong> the binary system<br />

Empirical expressions for calculation <strong>of</strong> viscosity <strong>of</strong> the system <strong>of</strong> a given type, which<br />

permit more precise calculations, are given in monograph. 3<br />

From [9.31], it follows that the relative temperature coefficient <strong>of</strong> viscosity<br />

βη = ∂η/ η∂T= ∂ln η/ ∂Tfor<br />

mixtures <strong>of</strong> chemically non-interacting liquids is described by<br />

equation:<br />

( )<br />

β = xβ + 1 −x<br />

β<br />

[9.32]<br />

η η1 η2

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