Examples of 'twin-screw extruder' in a sentence
Meaning of "twin-screw extruder"
A twin-screw extruder is a machine used in the process of compounding, mixing, and extrusion of various materials like plastic, rubber, and food products
How to use "twin-screw extruder" in a sentence
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twin-screw extruder
The use of a twin-screw extruder is preferred.
The extruder is preferably a twin-screw extruder.
A twin-screw extruder of high shear type is preferable.
A preferable kneading machine is a twin-screw extruder.
Methods in which a twin-screw extruder is used are preferred.
The pellets were obtained by extrusion in a twin-screw extruder.
Either a single or twin-screw extruder may be used.
A twin-screw extruder of high shear type is particularly preferred.
In the present invention a twin-screw extruder is preferred.
A corotating twin-screw extruder was used to get glycerol plasticized caseinate pellets.
The blend is introduced into a twin-screw extruder.
A twin-screw extruder is particularly preferred for the handling of fine powders.
The mixture then was compounded in a twin-screw extruder.
The twin-screw extruder had one kneading zone before a vent.
Compounding or mixing in a twin-screw extruder is one of these processes.
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Such a homogeneous mixture can be obtained from a twin-screw extruder.
The volatilizer can be a twin-screw extruder or a membrane vaporizer.
This mixture is then gelled in an internal mixer or a twin-screw extruder.
The devolatilizer may be a twin-screw extruder or a film evaporator.
Samples of the premixes were fed separately to the twin-screw extruder.
Said mixture was introduced into a twin-screw extruder and extruded through a 3 mm die.
The extrusion is preferably carried out by means of a twin-screw extruder.
However, a single twin-screw extruder is preferably used to perform the entire process.
The extrusion is carried out using a twin-screw extruder.
Therefore, the method using a twin-screw extruder is now described in further detail.
The cooker extruder used can be a single or a twin-screw extruder.
A unit such as a twin-screw extruder would be an example of a suitable piece of mixing equipment.
All of the components are compounded in the twin-screw extruder at conventional conditions.
Step a is preferably performed in an extruder and more preferentially in a twin-screw extruder.
The mixture was melt-kneaded with a twin-screw extruder to give a pelletized composition.
Processing was carried out by melt mixing by means of a co-rotating twin-screw extruder.
The use of a twin-screw extruder results in high shear mixing in localized areas.
Polymer pellets were fed into the hopper of the twin-screw extruder.
Preferably a corotating twin-screw extruder exhibiting one or more vent sections is used.
This mixing is preferably performed in an extruder, most preferably a twin-screw extruder.
However, a single twin-screw extruder is preferably employed to conduct the entirety of the process.
The powder blend was fed into the hopper of a twin-screw extruder.
Alternately, and preferably a twin-screw extruder can be employed to get the final compound.
The homogeneous dispersion is preferably achieved in an extruder, preferably in a twin-screw extruder.
The mixtures were respectively kneaded with a twin-screw extruder to prepare kneaded pellets.
Particular preference is given to the design as a closely intermeshing, corotatory twin-screw extruder.
The powdery mixture was then fed into a twin-screw extruder and was melt-extruded.
Polymers were mixed with suitable plasticizers to enable processing with a twin-screw extruder.
Among them, a twin-screw extruder equipped with a side feeder is most preferably used.
Preference is given to using melt extrusion, for example in a twin-screw extruder.
Particular preference is given to a twin-screw extruder having screws rotating in the same direction.
Suitable preparation equipment is for instance a single-screw or twin-screw extruder.
Where a twin-screw extruder is used, the halogenated copolymer is first ground into pellets.
The resulting cured sheets were granulated, then compounded on a twin-screw extruder.
The composition thus obtained is fed to a twin-screw extruder where it is melted and mixed.
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The use of a twin-screw extruder is preferred
The extruder is preferably a twin-screw extruder
Corotating twin-screw extruders are particularly preferred
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An extruder is advantageously used to prepare the mixture
