Unterschiede
Hier werden die Unterschiede zwischen zwei Versionen angezeigt.
| Beide Seiten der vorigen RevisionVorhergehende ÜberarbeitungNächste Überarbeitung | Vorhergehende Überarbeitung | ||
| en:grundlagenhandbuch:entgasungsoberflaechenberechnung:entasungseffizienz [2025/06/26 11:43] – deppe2 | en:grundlagenhandbuch:entgasungsoberflaechenberechnung:entasungseffizienz [2026/01/28 10:40] (aktuell) – gelöscht deppe2 | ||
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| - | ====== Degassing efficiency of the process ====== | ||
| - | ===== Degassing efficiency of the process ===== | ||
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| - | The degassing efficiency is evaluated with the degassing reference parameter of Schuler (Equation 1. In this case taken place the determination for wetting and non-wetting polymer. | ||
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| - | $$\frac{c_{Start} - c_{End}}{c_{Start} - c_{Gleichgewicht}} = \frac{\left(\frac{A_{POOL}}{t_{POOL}} + \frac{A_{FILM}}{t_{FILM}} + \frac{A_{GRUND}}{t_{GRUND}}\right)}{\dot{m}} \text{Equation 1}$$ | ||
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| - | After transposing of the equation can be the end concentration of low molecular component determined. Thereby is it possible to take a statement about the degassing efficiency. | ||
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| - | For wetting polymer is the Equation 2and for non-wetting polymer is the Equation 3 used. | ||
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| - | $$EK_{Benetzend} = \frac{\left(\frac{A_{POOL}}{t_{POOL}} + \frac{A_{FILM}}{t_{FILM}} + \frac{A_{GRUND}}{t_{GRUND}}\right)}{\dot{m}} \text{Equation 2}$$ | ||
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| - | $$EK_{Nicht-Benetzend} = \frac{\left(\frac{A_{POOL}}{t_{POOL}} + \frac{A_{FILM}}{t_{FILM}}\right)}{\dot{m}} \text{Equation 3}$$ | ||
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| - | The difference between both equation is that the surface area und renewal time at screw root is neglected, because in non-wetting case are not melt at screw root available. | ||