Unterschiede
Hier werden die Unterschiede zwischen zwei Versionen angezeigt.
| Beide Seiten der vorigen RevisionVorhergehende ÜberarbeitungNächste Überarbeitung | Vorhergehende Überarbeitung | ||
| en:berechnungen:temperaturverlauf [2024/07/29 17:25] – neelest | en:berechnungen:temperaturverlauf [2026/09/17 16:04] (aktuell) – gelöscht - Externe Bearbeitung (Unbekanntes Datum) 127.0.0.1 | ||
|---|---|---|---|
| Zeile 1: | Zeile 1: | ||
| - | ======Temperature profile====== | ||
| - | |||
| - | FIXME | ||
| - | |||
| - | ===== Theoretical principles of temperature calculation ===== | ||
| - | |||
| - | REX calculates the temperature in the melt vortex and in the melt film for each interval after the [[en: | ||
| - | |||
| - | The temperature calculation is based on the gutter model. The following conditions are assumed for the temperature curve calculation: | ||
| - | |||
| - | * The screw channel is considered a flat channel, i.e. $b \gg h$. The influence of the webs can therefore be neglected | ||
| - | * The melt adheres to the wall | ||
| - | * The temperature of the melt at the cylinder corresponds to the cylinder temperature | ||
| - | * The flow is laminar creeping and incompressible | ||
| - | * The flow behaviour of the melt should follow the power law $\tau = K * \dot \gamma^n$ | ||
| - | * All material values with the exception of viscosity are considered (interval-wise) to be temperature-independent. Provided the temperature range is not too large, this assumption is permissible for plastic melts to a reasonable approximation. This applies in particular to thermal conductivity and thermal diffusivity | ||
| - | |||
| - | The resulting differential equation can now be applied interval by interval and the temperature of the plastic melt in the melt vortex can be calculated [[en: | ||
| - | |||