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Investigations of the Residence Time and the Longitudinal Mixing Behavior in Counter-rotating Twin Screw Extruders
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H. Potente
and S. M. Schultheis
Published/Copyright:
May 27, 2013
Abstract
This paper presents a distribution function which allows to calculate the residence time distribution in a counter rotating twin screw extruder. Only the minimum and mean residence time appear in this function. The agreement between calculated and experimentally determined residence times is satisfactory. Longitudinal mixing capacity is discribed with the aid of the residence time variance.
Published Online: 2013-05-27
Published in Print: 1989-12-01
© 1989, Carl Hanser Verlag, Munich
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Articles in the same Issue
- Contents
- Contents
- Original Contributions
- New Aspects in the Design of Extruders with a Forced Feeding Section
- Flow of Rubber Compound in a Pin Barrel Screw Extruder
- Foam Processing with Rigid Polyvinylchloride
- A Model for Single-screw Plasticating Extruders
- Effect of Screw Stagger on Mixing in a Tangential Counter-Rotating Twin Screw Extruder
- Mixing, Devolatilization, and Reactive Processing in the a Farrel Continuous Mixer**
- Investigations of the Residence Time and the Longitudinal Mixing Behavior in Counter-rotating Twin Screw Extruders
- Flow in a Modular Intermeshing Co-rotating Twin Screw Extruder
- Continuous Melt Polymerization of Polyetherimides
Articles in the same Issue
- Contents
- Contents
- Original Contributions
- New Aspects in the Design of Extruders with a Forced Feeding Section
- Flow of Rubber Compound in a Pin Barrel Screw Extruder
- Foam Processing with Rigid Polyvinylchloride
- A Model for Single-screw Plasticating Extruders
- Effect of Screw Stagger on Mixing in a Tangential Counter-Rotating Twin Screw Extruder
- Mixing, Devolatilization, and Reactive Processing in the a Farrel Continuous Mixer**
- Investigations of the Residence Time and the Longitudinal Mixing Behavior in Counter-rotating Twin Screw Extruders
- Flow in a Modular Intermeshing Co-rotating Twin Screw Extruder
- Continuous Melt Polymerization of Polyetherimides