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Blow-molding exhaust time

Some time earlier, Eastman-Kodak has been working on a novel polyester as an entry into the important polyester fiber market and had devised a new ahcychc diol, 1,4-cydohexanedimethanol [105-08-5] effectively made by exhaustive hydrogenation of dimethyl terephthalate. Reaction of the new diol with dimethyl terephthalate gave a crystalline polyester with a higher melting point than PET and it was introduced in the United States in 1954 as a new polyester fiber under the trade name Kodel (5). Much later the same polyester, now called PCT, and a cyclohexanedimethanol—terephthalate/isophthalate copolymer were introduced as mol ding resins and thermoforming materials (6). More recentiy stiU, copolymers of PET with CHDM units have been introduced for blow molded bottie resins (7). [Pg.293]

Rocker bottoms Blowing air not vented before mold opens Insufficient cooling Increase air exhaust time Clean mold cooling channels Increase blow time... [Pg.205]

Check exhaust-possibly add exhaust time Check core rod openings Increase blow pressure Check core rod openings Reduce injection pressure Increase temperature in parison mold at fold location... [Pg.815]


See other pages where Blow-molding exhaust time is mentioned: [Pg.116]    [Pg.116]    [Pg.117]    [Pg.272]    [Pg.737]   
See also in sourсe #XX -- [ Pg.116 ]




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