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5.3.4.2 Amorphous Polymers<br />

Amorphous polymers do not exhibit the sharp enthalpy change as crystalline plastics<br />

when passing from liquid to solid. Consequently, when applying the numerical method<br />

of SCHMIDT [24], the correction for the latent heat can be left out in the calculation.<br />

A sample plot calculated with the computer program given in [3] is shown in Figure 5.44<br />

for amorphous polymers.<br />

It is to be mentioned here that the analytical solutions for non-steady heat conduction<br />

given in Section 3.2.1 serve as good approximations for crystalline as well as for<br />

amorphous polymers.<br />

5.3.5 Design of Cooling Channels<br />

5.3.5.1 Thermal Design<br />

In practice, the temperature of the mold wall is not constant, because it is influenced by<br />

the heat transfer between the melt and the cooling water. Therefore, the geometry of the<br />

cooling channel lay out, the thermal conductivity of the mold material, and the velocity<br />

of the cooling water affect the cooling time significantly.<br />

The heat transferred from the melt to the cooling medium can be expressed as (Figure<br />

5.45)<br />

The heat received by the cooling water in the time tK amounts to<br />

(5.89)<br />

(5.90)<br />

The cooling time tK in this equation can be obtained from Equation 3.41. The influence<br />

of the cooling channel lay out on heat conduction can be taken into account by the shape<br />

factor Se according to [23, 26].<br />

Figure 5.45 Geometry for the thermal design of cooling channels

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