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Blenders extruders

The major situations are gas-solid, gas-liquid, liquid, and solids. Solids blending can include dry solids blenders extruders for foodstuffs and polymers and pug mills for clays, thick pastes, and fertilizers. [Pg.1426]

Processing line, upstream Refers to material movement and auxiliary equipment (dryer, mixer/blender, storage bins, etc.) that exist prior to plastic entering the main fabricating machine such as the extruder. [Pg.641]

Mineral-filled nylon 6/6 composites. Kaolin (Burgess) was treated with the appropriate silane in a Patterson Kelly 8-qt. twin shell blender with intensifier bar. Treatment levels were 1% active silane. The kaolin was compounded with nylon 6,6 (Vydyne 21x—Monsanto) in a Leistritz twin screw extruder. The compounds were tested in a dry as molded condition in accordance with ASTM D-638 (see Table 5). [Pg.103]

Polystyrene family GPS, HIPS, SAN, ABS Solid concentrates, some intensive blends Internal mixers, continuous mixers, multiple-screw extruders, high-speed dry blenders... [Pg.151]

Central Blending Mixing the colorant system with polymers in a low-intensity blender at a central plant location, then conveying that blend pneumatically or by bulk container to the molding machine or extruder. [Pg.263]

For the mechanical blending in an extruder, particles of PBT and EPR were dried in a vacuum oven at, respectively, 120°C and at RT for 3 h. The components were first mixed in a high-speed blender, then extruded in a single-screw machine and pelletized. During the extrusion, a small amount of DCP was added to crosslink EPR. DCP did not affect the properties of the blend, although it eliminated the delamination. The surface of the sample was coarse. [Pg.813]

All materials were dry blended together in a high speed blender following the predesigned composition ratios. Then a corotating twin-screw extruder (SHJ-30, diameter 30 mm) was employed at a screw speed of 110 rpm and barrel temperatures... [Pg.558]

Following the dissolution step, the viscose is carefully blended to achieve the best uniformity of properties according to the process used, continuous or batch. From the blender, the viscose is filtered in a number of steps to remove undissolved particles and contaminants. Durso and Parks have reviewed the early work on viscose filtration [155]. The primary objective of filtration is to remove particles that would plug spinnerette holes and cause fiber defects. Because of the deformable nature of many viscose particles, it is impossible to remove all of them by filtering some will be extruded and others break up into smaller particles [156,157]. Research on the effects of such particles that might be extruded is expected to lead to significant advances in the control of fiber quality [158]. [Pg.725]

For the first group the following types of dryers are generally used convective (tray, band, fluid bed, flash dryers, and their modifications) or contact (vacuum dryers such as double-cone dryer-blender, conical dryer with rotating helical mixer, paddle dryer). Pastelike materials are dried in tray dryers, band dryers equipped with extruding devices, and spin-flash dryers. Finally, thin pastes can be dried in spray dryers or on fluid beds or spouted beds of inert particles. Small amounts of solutions and suspensions are generally freeze-dried, especially if the product is thermolabile. [Pg.682]


See other pages where Blenders extruders is mentioned: [Pg.2661]    [Pg.2661]    [Pg.1647]    [Pg.350]    [Pg.189]    [Pg.90]    [Pg.1367]    [Pg.144]    [Pg.171]    [Pg.84]    [Pg.216]    [Pg.216]    [Pg.219]    [Pg.219]    [Pg.230]    [Pg.1468]    [Pg.741]    [Pg.754]    [Pg.1722]    [Pg.1969]    [Pg.1040]    [Pg.34]    [Pg.124]    [Pg.341]    [Pg.605]    [Pg.616]    [Pg.1957]    [Pg.818]    [Pg.1651]    [Pg.52]    [Pg.113]    [Pg.114]    [Pg.163]    [Pg.357]    [Pg.442]    [Pg.238]   
See also in sourсe #XX -- [ Pg.169 ]




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