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Kneading section

The screw of standard design (Fig. 7) normally comprises a through shaft mounting in a predetermined succession different screw bushes (elements) and special kneading sections composed of discs turned relative to one another. [Pg.151]

Fig. 5.15 Evidence of melting of fine particulates of PP powder melted in a 30-mm Co-TSE, taking place in the partially filled kneading section. Such molten fines are capable of creating, as glue points, particulate clusters. [Reprinted by permission from M. Esseghir, D. W. Yu, C. G. Gogos, and D. B. Todd, SPE ANTEC Tech Papers, 43, 3684 (1997).]... Fig. 5.15 Evidence of melting of fine particulates of PP powder melted in a 30-mm Co-TSE, taking place in the partially filled kneading section. Such molten fines are capable of creating, as glue points, particulate clusters. [Reprinted by permission from M. Esseghir, D. W. Yu, C. G. Gogos, and D. B. Todd, SPE ANTEC Tech Papers, 43, 3684 (1997).]...
We now turn our attention to PED. As mentioned earlier, individual pellets become grossly deformed while in compacted assemblies, for example, in kneading sections of the Co-TSE. These volumewise particulate deformations make the particulate assemblies active participants in the process of melting through the mechanism of PED. Two questions must be addressed (a) how powerful a heat source term is PED and (b) how can the complex reality of compacted particulate assemblies undergoing large and repeated deformations be described and simulated mathematically ... [Pg.221]

The extruder can be fed with a paste or a dry powder. In the case of a dry powder the extruder will have a kneading section where a liquid is add to the powder and the powder is kneaded to a paste. In the other case the paste is made in a separate kneader before feeding it into the extruder. The rheological properties of the paste are very important, so the formulation of the paste is the most... [Pg.328]

Twin-screw extruder The kneading section (independentiy of its construction), further reduced the drop diameter by a factor of ten. Experimental and theoretical. Non-isothermal model with drop diameter de Loor et al., 1994,... [Pg.599]

Co- or counter-rotating and elongation rates and adiabatic T-gradient were computed for the conveying and kneading sections. A 3D modeling of flow in fuU conveying screw elements of either a CORI Kajiwara et al. 1996... [Pg.599]

Figure 5.24 Modular assembly ofscrew and sectionized barrel (highlighting the kneading section and gear mixer section). Courtesy of KraussMaffei Berstorff [10. ... Figure 5.24 Modular assembly ofscrew and sectionized barrel (highlighting the kneading section and gear mixer section). Courtesy of KraussMaffei Berstorff [10. ...
In addition to a regular co-rotating intermeshing twin-screw extruder system, which is analogous to the above-mentioned twin-screw extruder systems, Japan Steel Works (www.jsw.co.jp) has patented a special modification for a TSE barrel and screw kneading section to enhance the polymer blend qualities, as presented in the following subsections. [Pg.223]

Material-Barrel Temperature HDPE powder melted before the kneading block because of the heat transfer from the 200°C barrel, whereas the porous PP pellets were only partially molten before the kneading section. Hence, the HDPE conversion to grafted GMA occurred in the upstream screw conveying section. [Pg.341]

Kneading section Kneading section Kneading section... [Pg.358]

What s New in Compounding Extrusion. Plastics Formul Compound 2 16-30, 1996. MA Huneault, MF Champagne, A Luciani. Polymer blend mixing and dispersion in the kneading section of a twin-screw extruder. Polym Eng Sci 36 1694-1706, 1996. DB Todd. SPE Preprints. New York Antec 89, 1989, p 168. [Pg.365]

Figure 11.5 Screw lay out of the corotating extruder. Trl 0.225-m transporting section, Prl 0.15-m pressure build-up section, Kn 30° 0.09-m kneading section with 30° forwarding angle, Kn. —30° 0.09-m kneading section with 30° reversed angle, Tr2 0.48-m transporting section, Pr2 0.15-m pressure build-up section. Figure 11.5 Screw lay out of the corotating extruder. Trl 0.225-m transporting section, Prl 0.15-m pressure build-up section, Kn 30° 0.09-m kneading section with 30° forwarding angle, Kn. —30° 0.09-m kneading section with 30° reversed angle, Tr2 0.48-m transporting section, Pr2 0.15-m pressure build-up section.

See other pages where Kneading section is mentioned: [Pg.154]    [Pg.453]    [Pg.499]    [Pg.601]    [Pg.811]    [Pg.954]    [Pg.957]    [Pg.222]    [Pg.245]    [Pg.328]    [Pg.214]    [Pg.7]    [Pg.57]    [Pg.144]    [Pg.8]    [Pg.283]    [Pg.167]    [Pg.168]    [Pg.169]    [Pg.170]    [Pg.236]    [Pg.136]    [Pg.136]    [Pg.229]   
See also in sourсe #XX -- [ Pg.167 , Pg.170 ]




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KNEADING

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