Polyurethane prepn - from polyisocyanates, polyether-, polyesterpolyols and transesterified polyols

    公开(公告)号:DE2457726A1

    公开(公告)日:1976-06-16

    申请号:DE2457726

    申请日:1974-12-06

    Applicant: BASF AG

    Abstract: (Cellular)polyurethanes are prepd. from a mixt. of A) >=1 polyisocyanate, B) >=1 polyhydroxy cpd. of mol. wt. 500-7,000 chosen from polyether-and polyester-polyols and opt. D) other conventional additives, the novelty being that a polymer (C) is included in the mixt.; C) is the reaction prodt. of a polymer contg. >=1 gp. capable of (trans)esterification and a polyhydroxy cpd. chosen from polyester- or polyether-polyols of mol. wt. 200-7,000 with formation of at least a partial ester like bond. Polymers contg. covalently bonded polyhydroxy cpds., useful in polyurethane chemistry are easily obtd. cf. prior art where either a) polyhydroxy cpds. and polyisocyanates were reacted or b) in situ free radical graft polymers contg. polyetherpolyols grafted over C-C bonds were used. Physical props. e.g., load capacity and low temp. flexibility are also improved. As flexible or rigid, foams, elastomers or coatings. The foams may be used as shoe soles, or in the automobile industry.

    3.
    发明专利
    未知

    公开(公告)号:DE2613352A1

    公开(公告)日:1977-10-06

    申请号:DE2613352

    申请日:1976-03-29

    Applicant: BASF AG

    Abstract: A process for the manufacture of high impact and translucent polystyrene, in which, in a first stage, styrene is prepolymerized in mass or in solution in the presence of a rubber, and the polymerization is then completed in mass, in solution or in aqueous suspension. The prepolymerization is taken to a stage where the amount of styrene converted is from 3 to 10 times the amount of the elastomer constituent of the rubber, and at this conversion the disperse soft-component phase formed should have a mean particle size of less than 1 mu m and should contain from 35 to 65% by weight of free or chemically bonded polystyrene segments. The translucent styrene polymers of high impact strength may be used for packaging purposes.

    5.
    发明专利
    未知

    公开(公告)号:DE3030055A1

    公开(公告)日:1982-03-25

    申请号:DE3030055

    申请日:1980-08-08

    Applicant: BASF AG

    Abstract: A process for the preparation of ethylene homopolymers, and ethylene copolymers with minor amounts of higher alpha -monoolefins, by polymerizing the monomer or monomers by means of a supported catalyst (1) containing a chromium-hydrocarbon complex (1.2) on an inorganic oxide carrier (1.1), wherein (1) a supported catalyst is employed which contains (1.2) a chromium-hydrocarbon complex of the formula RCrACrR, where R is a cyclic and/or open-chain hydrocarbon, or hydrocarbon radical, of 2n and 2n+1 carbon atoms respectively and having from 1 to n non-cumulated double bonds, n being from 2 to 10, Cr is chromium and A is cyclooctatetraene, a divalent n-octatetraene radical or alkyl-substituted homologs thereof, on (1.1) a particular inorganic oxide carrier, with or without (2) a co-catalyst chosen from a particular group of alkyl-aluminum compounds. The process gives polymers having a particularly broad molecular weight distribution.

    Block copolymer from anionic and radical polymerisable monomers - using di-halogenated azo cpds.

    公开(公告)号:DE2546377A1

    公开(公告)日:1977-04-21

    申请号:DE2546377

    申请日:1975-10-16

    Applicant: BASF AG

    Abstract: Prepn. of block copolymers from a polymer block (a) from anionic-polymerisable monomer (a) and one or two polymer blocks (B) from radical-polymerisable monomer (b), is described. The process comprises (1) coupling of block (A) with one or two end alkali metal-carbon bonds with an azo cpd. of formula X-(CH2)n-C(R1R2)-N N-C(R1R2)- - (CH2)n-X (I) where X is Cl or Br, R1 and R2 are 1-20C aliphatic, cycloaliphatic or aromatic gps.; n is 0-5) (2) addn. of (b) and heating to decompose the coupling prod. and give a block (A) with one or two radical chain ends, and (3) polymerisation of blocks (B) or to one or both chain ends. Molar ratio of alkali metal in (A) to halogen in (I) is pref. 1:1. Impact-resistant copolymers, e.g. of SAN or ABS type, may be obtd. Yield and mechanical properties of the prodn. are improved by use of (I) in place of azodinitriles.

    Ethylene (co)polymerisation carrier catalyst prepn. - by coating porous finely-divided silica-alumina support with chromium hydrocarbon complex cpd.

    公开(公告)号:DE3030916A1

    公开(公告)日:1982-04-08

    申请号:DE3030916

    申请日:1980-08-16

    Applicant: BASF AG

    Abstract: In the prepn. of a new carrier catalyst, contg. a Cr-hydrocarbon complex cpd. on an inorganic oxide carrier, a Cr hydrocarbon-complex cpd. having formula RCrACrR (where R is a hydrocarbon or a ring- and/or open-chained hydrocarbyl gp. contg. 2 n or 2n + 1C atoms and 1-n non-heaped double bonds; n is integer 2-10 and A is cyclooctatetraene or a divalent n-octatetraene gp. in either of which up to 8 H atoms can be substd. by 1-4C alkyl gps.) is applied to a finely-divided, porous, inorganic-oxidic carrier. The carrier has particle dia. 1-1000 microns, pore vol. 0.3-3 cc/g, surface 100-1000 sq.m/g and formula SiO2.aAl2O3 (where a is no. 0-2). The carrier catalyst (I) whould contain 0.01-10 wt.% w.r.t. carrier (1,1), of complex cpd. (1,2), calculated as Cr. The catalyst is used in C2H4 homo-polymerisation or co-polymerisation with alpha-mono-olefins. Polymers can be obtd. having a wide mol.wt. distribution.

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