Unterschiede
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| en:berechnungen:wandgleitende_materialien [2024/10/25 17:06] – alte Version wiederhergestellt (2024/10/17 20:24) neelest | en:berechnungen:wandgleitende_materialien [2026/07/14 09:55] (aktuell) – cschall | ||
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| - | ======Wall-slipping | + | ======Wall-slipping |
| - | The content is currently being processed | + | When considering flow processes in rheometers, but also in practical components such as dies, plasticizing units, |
| - | ===== Wall-slipping | + | |
| - | When considering | + | When the transition from wall adhesion to wall slip occurs, most equations used to calculate a flow are no longer valid. Since this is a very complex phenomenon that depends on viscosity, shear rate, shear stress, temperature, and pressure, a simple and stable empirical model is used. |
| - | such as dies, plasticating units and between gaps, the flowing melt is presumed | + | |
| - | wall adhering. In polymer melting | + | |
| - | However, there are some materials, among which the ultrahigh molecular | + | |
| - | polyethylene of high density (HDPE) | + | |
| - | (PVC, frequently provided with outward lubricants for a gentle processing), | + | |
| - | wall slipping under certain conditions. | + | |
| - | In order to calculate | + | Due to the complex relationships involved, |
| - | **PSI**, the option “wall slipping” has been added in the software. For this, critical | + | |
| - | Chapter Rheological Material Data. | + | |
| - | When choosing the menu item Wall slipping, **REX/PSI** considers that wall slipping | + | In REX/PSI, wall slip occurs above a critical shear stress. |
| - | occurs above the critical | + | |
| - | wall and the root surface are evaluated and limited to a value whose maximum is | + | |
| - | equal to the critical shear stress | + | |
| - | $$τ_ {WH,S} > τ_{krit} ⇒ τ_S = τ_{krit}$$ | + | For the dissipation calculation, the following applies: |
| - | This limitation affects the flow profile in the screw channel and decreases the local | + | $$ \tau_0 = \eta_0 \cdot \dot{\gamma} $$ |
| - | pressure gradient. Thus, the pressure build-up capacity decreases but also the | + | $$ if $$ |
| - | pressure consumption of overridden screw sections. | + | $$ \tau_0 > \tau_{crit}(T) $$ |
| + | $$ then $$ | ||
| + | $$ \Delta \tau = \tau_0 | ||
| + | $$ \tau_{target} = \tau_{crit}(T) + \Delta \tau \cdot k_{mat} $$ | ||
| + | $$ with $$ | ||
| + | $$ 0 < k_{mat} \leq 1 $$ | ||
| + | $$ it~follows~that $$ | ||
| + | $$ \eta_{wall~slipping} = \frac{\tau_{target}}{\dot{\gamma}} $$ | ||
| - | **Platzhalter Abb. 9.36: Druckverlauf mit und ohne Wandgleiten** | + | If the local shear stress is greater than the critical shear stress, the shear stress is reduced by means of the factor $k_{mat}$. A value of $0$ corresponds to a hard limit at $\tau_{krit}$, |
| + | |||
| + | **Important: | ||
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| + | If wall slip is checked in the material data, the values entered there are used. If wall slip is unchecked there, wall slip is still calculated using predefined values, since experience has shown that, especially for high-viscosity polymers with correspondingly high shear stresses, an excessively high temperature would otherwise be calculated. The default values used in this case are a critical shear stress of $\tau_{krit}=100 kPa$ and $k_{mat}=0, | ||
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| + | ===Further topics=== | ||
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