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    • 1. 发明授权
    • Mixing process for producing polyurethane plastics
    • 用于生产聚氨酯塑料的混合工艺
    • US3141865A
    • 1964-07-21
    • US66539857
    • 1957-06-13
    • ALLIED CHEM
    • MCEVOY RICHARD T
    • B29B7/40B29C44/34B29C44/36
    • B29C44/36B29B7/408B29C44/3442
    • A mixing apparatus and process (see Division B1) may be used for the continuous preparation of low-density flexible polyurethane foams. In an example a polyisocyanate is added to a mixture of polyol, water, catalyst, emulsifier and colourant. The polyisocyanate was a mixture of m-tolylene diisocyanate containing 80% of the 2, 4 isomer and 20% of the 2, 6 isomer; the polyol was prepared by copolymerizing adipic acid with a glycol and a triol. The emulsifier was a polyethylene glycol ricinoleate; the catalyst, N-methyl morpholine, and the colourant a copper phthalocyanine filter cake. 2250 G/min of polyol premix and 900 G/min tolylene diisocyanate mixture were supplied to the mixer which was operated at 4,000 r.p.m. with residence time of 1 sec. The volume of the discharged reaction mixture increased 46-fold after 1 minute, and after curing provided a foam of density 1.6 lb./cu. ft. In another example the polyisocyanate and polyol components were pre-mixed and partially reacted to form a pre-polymer which was afterwards mixed with a catalyst mixture. The polyol was a mixture of adipic acid and diethylene glycol, and the polyisocyanate and catalyst were the same as in the first example. The pre-polymer was prepared by mixing 390 parts of tolylene diisocyanate mixture and 1,000 parts of the polyol and agitating for 30 minutes under an atmosphere of carbon dioxide. 2,840 G/min. of the pre-polymer and 200 G/min. of catalyst were supplied to the mixer under the same conditions as before. Volume expansion of the product was 35 fold and the cured foam has a density of 2.1 lb/cu. ft.