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The temperature dependence of liquid viscosity is usually expressed by one of the following models:

Exponential model


\mu(T)=\mu_0 \exp(-bT)

where T is temperature and \mu_0 and b are coefficients. See first-order fluid and second-order fluid. This is an empirical model that usually works for a limited range of temperatures.

Arrhenius model


The model is based on the assumption that the fluid flow obeys the Arrhenius equation for molecular kinetics:

\mu(T)=\mu_0 \exp( \frac {E}{RT} )

where T is temperature, \mu_0 is a coefficient, E is the activation energy and R is the universal gas constant. A first-order fluid is another name for a power-law fluid with exponential dependence of viscosity on temperature.

WLF model


The Williams-Landel-Ferry model or WLF for short is usually used for polymer melt's or other fluids that have a glass transition temperature.

The model is:

\mu(T)=\mu_0 \exp \left( \frac {-C_1 (T-T_r)} {C_2+ T -T_r} \right)

where T-temperature, C_1, C_2, T_r and \mu_0 are empiric parameters (only three of them are independent from each other).

If one selects the parameter T_r based on the glass transition temperature, then the parameters C_1, C_2 become very similar for the wide class of polymers. Typically, if T_r is set to match the glass transition temperature T_g, we get

C_1 \approx17.44

and

C_2 \approx51.6 K.

Van Krevelen recommends to choose

T_r=T_g+43 K, then

C_1 \approx8.86

and

C_2 \approx101.6 K.

Using such universal parameters allows one to guess the temperature dependence of a polymer by knowing the viscosity at a single temperature.

In reality the universal parameters are not that universal, and it is much better to fit the WLF parameters from the experimental data.

Non-Newtonian fluids

 

This article is licensed under the GNU Free Documentation License. It uses material from the "Temperature dependence of liquid viscosity".

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