Unterschiede
Hier werden die Unterschiede zwischen zwei Versionen angezeigt.
| Beide Seiten der vorigen RevisionVorhergehende ÜberarbeitungNächste Überarbeitung | Vorhergehende Überarbeitung | ||
| en:berechnungen:temperaturverlauf [2024/10/17 20:11] – [Influence of the internal temperature control on the temperature] neelest | en:berechnungen:temperaturverlauf [2026/09/17 16:04] (aktuell) – gelöscht - Externe Bearbeitung (Unbekanntes Datum) 127.0.0.1 | ||
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| - | ======Temperature profile====== | ||
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| - | ===== Theoretical principles of temperature calculation ===== | ||
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| - | REX calculates the temperature in the melt vortex and in the melt film for each interval after the [[en: | ||
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| - | The temperature calculation is based on the gutter model. The following conditions are assumed for the temperature curve calculation: | ||
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| - | * 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 | ||
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| - | 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: | ||
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| - | ==== Temperature calculation in PSI ==== | ||
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| - | In addition, a proportional downtime is taken into account for each interval in PSI. The procedure is very similar to the consideration of downtimes during [[en: | ||
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| - | For the calculated downtime weighted per interval, heating is calculated purely by heat conduction through the cylinder temperature control. The more downtime the plastic experiences between entering the injection moulding machine and injection, the closer the temperature curve comes to the heating zone profile. | ||
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| - | ===== Special features in the temperature calculation ===== | ||
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| - | There are two special cases that affect the temperature calculation. These are disperse melting and the internal tempering of a screw. | ||
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| - | ==== Influence of disperse melting on the temperature ==== | ||
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| - | If [[en: | ||
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| - | {{ : | ||
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| - | The heat flow causes the melt to cool down: | ||
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| - | $\Delta T = \frac{\dot q_{particle} * N * t}{c_p * V_{melt} * \rho}$ | ||
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| - | with the heat flow per particle $\dot q_{particle}$, | ||
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| - | At the same time, the solid particles in the channel result in a reduced effective channel height, which leads to a locally increased shear rate in the melt: | ||
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| - | $\dot \gamma = \frac{v_{0, | ||
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| - | $\dot \gamma = \frac{v_{0, | ||
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| - | with $v_{0,z}$ as the circumferential velocity, the channel height $h$, the particle diameter $d_{particle}$ and the number of particles at channel height $N_{height}$ | ||
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| - | The temperature reduction and the simultaneously higher shear rate counteract each other, so that different behaviour can occur depending on the process. As a rule, however, the cooling of the melt predominates, | ||
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| - | < | ||
| - | * Pape, Jens: Fundamentals of process simulation of single-screw concepts for high-performance plasticising, | ||
| - | * Dörner, Marius: Wave screws in single-screw extrusion, dissertation, | ||
| - | </ | ||
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| - | ==== Influence of the internal temperature control on the temperature ==== | ||
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| - | The internal temperature control is calculated iteratively. \\ | ||
| - | First, the temperature curve without internal temperature control is always calculated. The steady-state heat flows for the constant screw base temperature profile can be calculated from the known volume flow of the temperature control medium, the geometry and thermal conductivity of the screw and the inner tube as well as the known screw base temperature. \\ | ||
| - | The temperature calculation is then carried out again, taking into account the heat flow into the tempered screw core. The resulting temperature reduction only occurs at the base of the screw and leads to an inhomogeneous temperature profile over the channel height. As a result, a cooler screw base temperature is calculated, which in turn is used to calculate the heat flows in the tempering medium and within the screw. \\ | ||
| - | With the heat flow into the screw core now reduced, the temperature calculation is started again. The process is carried out iteratively until a stationary process is reached. | ||
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| - | ===Further topics=== | ||
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