Also claimed is an extruder, in particular a large extruder for plastics processing, which is equipped with at least one bearing support according to the invention.
A system for the production of such a polycarbonate sheet includes an extruder, a co-extruder, an extrusion die, and a thermoformer.
The polymer material (6) is made in an extruder, preferably a double-worm extruder.
plasticating capacity of an extruder
plasticating capacity of an extruder
A die apparatus (18), a method of using the die apparatus to produce co-extruded polymeric articles, and co-extruded polymeric articles produced using the die apparatus and method are disclosed.
The method for the continuous production of a composition comprising rubber (20), hydrocarbon resin (22), and solvent (26) provides for the use of a dual-screw extruder (10), for example, a co-rotating dual-screw extruder.
The invention relates to a single screw extruder having a means for the introduction of additives and to a method of introducing additives into a silicone rubber composition in the aforementioned extruder.
The agglomerate is produced in an extruder, in particular a screw-feed extruder, to which the required amounts of gelatine and solids are supplied.
A multiple-screw extruder in which paired screws, or segments thereof, contain unequal numbers of flights; and a screw for use in such extruder.
An extruder screw (10) for use in a barrel of an extruder for forwarding thermoplastic polymer from a first end to a second end of the extruder.
Further the invention can comprise a single extruder or a co-extruder used to make a co-extruded product wherein uniform velocity becomes more desirable.
The apparatus further includes at least one secondary extruder (34), or co-extruder, for the extruding of each reclosable profile onto the tubing.
The apparatus further includes at least one secondary extruder (30, 34), or co-extruder, for the extruding of each reclosable profile onto the tubing.
In exemplary embodiments, the activated carbon is added to a primary extruder and water is directly injected into a secondary extruder.
A simulation apparatus, and program, for screw extruder volatilization, being capable of practical simulation of the volatilization process of screw extruder.
The present invention relates to an extruder for a polymer, and a process for extruding a polymer using said extruder.
Also provided are a straw roller extruder and a coal-straw mixed roller extruder used in the method for preparing the cylindrical granular fuel.
The first screw extruder, the composite roll set, and the second screw extruder are sequentially disposed on one side of a frame.
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