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3.1.2.1.1a) Arrhenius relation, flow activation energy EA, and Arrhenius curve

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An approximation model for kinetic activity in chemistry was developed in the general form by Svante A. Arrhenius (1859 to 1927) who introduced an activation constant (see also Chapter 14.2: 1884) [3.74]. The Arrhenius relation in the form of a η(T) fitting function describes the change in viscosity for both increasing and decreasing temperatures:

Equation 3.6

η(T) = c1 ⋅ exp (-c2 / T) = c1 ⋅ exp [(EA / RG) / T]

with the temperature T in [K], (i. e. using the unit Kelvin), and the material constants c1 [Pas] and c2 [K] of the sample (where c2 = EA / RG), the flow activation energy EA [kJ/mol], and the gas constant RG = 8.314 ⋅ 10-3 kJ / (mol ⋅ K)

Conversion between the temperature units:

Equation 3.7

T [K] = T [°C] + 273.15 K

At a certain temperature, the flow activation energy E A characterizes the energy needed by the molecules to be set in motion against the frictional forces of the neighboring molecules. This requires exceeding the internal flow resistance, with other words, a material-specific energy barrier, the so-called potential barrier [3.27].

The exponential curve function (Equation 3.6) occurs in a semi-logarithmic diagram as a straight line showing a constant curve slope if (1/T) is plotted on a linear scale on the x-axis (with the unit: 1/K), and η on a logarithmic scale on the y-axis. In this lg η / (1/T) diagram, the so-called Arrhenius curve, temperature-dependent behavior occurs as a downwardly or upwardly sloping straight line for a heating or a cooling process, respectively.

Note : Recommended temperature range for fitting functions (Arrhenius and WLF)

The Arrhenius relation is useful for low-viscosity liquids and polymer melts in the range of T > Tg + 100K (with the glass-transition temperature Tg, see Chapter 8.6.2.1a) [3.10] [3.34]. For analysis of polymer behavior at temperatures closer to Tg, it is better to use the WLF relation. For more information on this time/temperature shift method TTS, see Chapter 8.7.1.

The Rheology Handbook

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