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Extrusion, bleach processing

Table 3.12 shows that the melt flow index of HDPE in the presence of 50% wood flour decreases rather significantly, from 1.6 g/10 min for salt cedar to 0.2 g/10 min in the presence of pine. Fnrthermore, if we consider the initial MFI value for the neat plastic, a drop in MFI is qnite significant. For example, a polypropylene with MFI 23 g/10 min (MFI was 29 g/10 min after processing in the extruder at 100 or 300 rpm) was loaded with 20% bleached sulfite cellulose fibers, and after extrusion at 100 rpm MFI dropped to 2 g/10 min. With 30% loading with the fiber, MFI further decreased to 0.5 g/10 min [131]. [Pg.105]

Strong absorption of polysilanes in the UV region makes these materials suitable for application to photo (81) and X-ray lithography (82). Photo-bleaching by UV irradiation indicates scission as the major process for most polysilanes scission proceeds via silyl radical and/or silylene (R2Si ) extrusion (Fig. 9) (83). [Pg.6612]

PVDF copolymers at <1000 ppm in typical blown film applications is effective in reducing melt fracture and allowing increased extrusion rates Chemical resistance to bleaching agents and other paper mill process chemicals... [Pg.9054]

Highly suited for incontinence items. Thermally bonded laminates with cotton core and outer layer of MB and/or spunbonded (SB) webs process are designed by encapsulation of carded bleached cotton web with outer layers of MB PP and/or SB PP after extrusion process, prior to calendering. [Pg.477]


See other pages where Extrusion, bleach processing is mentioned: [Pg.644]    [Pg.292]    [Pg.11]    [Pg.98]    [Pg.20]    [Pg.395]    [Pg.330]    [Pg.4025]   
See also in sourсe #XX -- [ Pg.395 ]




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