Unterschiede
Hier werden die Unterschiede zwischen zwei Versionen angezeigt.
| Beide Seiten der vorigen RevisionVorhergehende ÜberarbeitungNächste Überarbeitung | Vorhergehende Überarbeitung | ||
| en:berechnungen:durchsatz [2024/10/30 13:16] – neelest | en:berechnungen:durchsatz [2026/09/17 09:24] (aktuell) – gelöscht - Externe Bearbeitung (Unbekanntes Datum) 127.0.0.1 | ||
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| - | ======Throughput====== | ||
| - | ===== Throughput ===== | ||
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| - | If the throughput or the metering time is specified in the processing parameters, | ||
| - | generally no recalculation of the throughput is conducted but all further calculations | ||
| - | will be conducted with the specified throughput. | ||
| - | |||
| - | As a standard feature, a linear temperature profile beginning at the front edge of the | ||
| - | hopper $T_G$ / $T_K$ and progressing to the point of the isothermal throughput calculation with | ||
| - | a specified melt temperature is assumed (see also [[en: | ||
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| - | Next, the reference zone is determined; this is the screw zone (no shear or mixing section) with the lowest channel depth. The reference zone is used to determine the average shear rate there. | ||
| - | The mean shear rate for this section is | ||
| - | obtained from the circumferential velocity, the screw back speed and the channel | ||
| - | depth. This shear rate is used to establish the current rheological material data. The | ||
| - | following approach is adopted here: | ||
| - | |||
| - | If the flow curve is available in the form of the Carreau data, a tangent is drawn to the | ||
| - | Carreau curve at the appropriate shear rate and temperature. The power law | ||
| - | parameters are then established for this tangent. | ||
| - | After these pre-calculations the actual throughput respectively metering time | ||
| - | calculations are conducted. | ||
| - | |||
| - | < | ||
| - | The vented screws are an exception here, where the location of the specified melt temperature is already set at the start of the degassing zone. The temperature curve then remains constant. | ||
| - | With venting extruders the throughput is calculated on the basis of the geometry of | ||
| - | the first screw stage, where the counterpressure at the venting point is set at 0 bar | ||
| - | corresponding to the physical conditions. | ||
| - | For vented screws, the reference zone must be located BEFORE the first degassing zone. | ||
| - | </ | ||
| - | |||
| - | In the first step, the total pressure difference (specified back pressure minus hopper pressure) is assumed for all screw zones (excluding shearing and mixing parts) and an initial mass flow rate is therefore determined. Based on this mass flow rate, the pressure loss across all shearing and mixing parts as well as the non-return valve (PSI only) is calculated and subtracted from the pressure difference so that a simplified linear pressure gradient is obtained across all feed, (de)compression, | ||
| - | |||
| - | < | ||
| - | At the beginning of the calculation of the metering time the screw is in the front screw | ||
| - | stage and will be retracted by 0.1* diameter. Thus, the length of the feed section is | ||
| - | cut by this amount and a new temperature profile is assigned to each screw stage. | ||
| - | The characteristic values of the throughput equation are determined for the screw | ||
| - | stage and the throughput is calculated afterwards. Using the cross sections of the | ||
| - | barrel the proportion between the screw back speed and the melt conveyed in the | ||
| - | screw vestibule enables the determination of the screw back speed. The required | ||
| - | metering time of 0.1 d for the shortening of the effective screw length can be | ||
| - | obtained by dividing the screw shift through the determined screw back speed. | ||
| - | In order to determine the entire metering time the single times for the metering path | ||
| - | divided into 0.1 D steps are added up. Besides the metering time the throughput for | ||
| - | the calculation point is defined, which is the basis for further calculations for this | ||
| - | screw stage. | ||
| - | </ | ||
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| - | The prerequisite for the throughput calculation is: | ||
| - | * A defined screw geometry that begins with a [[en: | ||
| - | * A defined [[en: | ||
| - | * The [[en: | ||
| - | * The [[en: | ||
| - | * The [[en: | ||
| - | * The [[en: | ||
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| - | ===Further topics=== | ||
| - | * [[en: | ||
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