11.
    发明专利
    未知

    公开(公告)号:DE19723003A1

    公开(公告)日:1998-12-03

    申请号:DE19723003

    申请日:1997-06-02

    Applicant: BASF AG

    Abstract: The invention relates to polymer mixtures containing at least 85 wt pct ethylene/ alpha -olefin copolymers (A) produced by metallocene catalysis and 1 to 15 wt pct essentially linear ethylene/ alpha -olefin copolymers (B) produced with a different catalyst, in relation to the total mass of the polymer mixture.

    Prepn. of vinyl]-aromatic polymers, giving syndiotactic polymers for use in prodn. of mouldings

    公开(公告)号:DE19506556A1

    公开(公告)日:1996-08-29

    申请号:DE19506556

    申请日:1995-02-24

    Applicant: BASF AG

    Abstract: Polymers of vinylaromatic cpds. are prepd. at 0-150 deg.C, in presence of catalysts contg. as active components (A) cpds. of formula XM(Z )z1(Z )z2(Z )z3 (I) and (B) (i) open-chain or cyclic alumoxane cpds. of formula (III) or (IV), or (ii) cpds. forming metallocene ions, comprising strong neutral Lewis acids, ionic cpds. with Lewis acid cations or ionic cpds. with a Bronsted acid as cation. In the formulae, X = 1-10C alkyl or alkoxy, 5-7 member cycloalkyl, 6-15C aryl or formula (II) (where R -R = H, 1-10C alkyl (opt. with 1-5 halogen substits.), 5-7 member cycloalkyl (opt. with 1-6C alkyl substits.), 6-15C aryl or arylalkyl where 2 vicinal gps. may together form 4-15C cyclic gps., or halogen, 1-10C alkoxy, NR R or Si(R )3 (where R , R = H, 1-10C alkyl, 6-15C aryl or 3-10C cycloalkyl); M = metal of the IInd - VIIIth Sub-gps.; Z -Z = polymers of vinylaromatic cpds., dienes, and/or acrylates; z1, z2, z3 = 0-3; z1 + z2 + z3 = 1-3; R = 1-4C alkyl; m = 5-30.

    15.
    发明专利
    未知

    公开(公告)号:DE4325824A1

    公开(公告)日:1995-02-02

    申请号:DE4325824

    申请日:1993-07-31

    Applicant: BASF AG

    Abstract: A process for the preparation of homopolymers of ethylene or copolymers of ethylene with secondary amounts of other C3- to C12-alk-1-enes by catalytic polymerisation in a suspension or in the gas phase in the presence of an antistatic at a temperature of from 50 to 120 DEG C and at a pressure of from 5 to 50 bar, characterised in that the antistatic employed is a mixture of the following substances: a) a metal salt of medialanic acid of formula (I) , b) a metal salt of an anthranilic acid of formula (II) , where the organic radical R is either alpha ) -CO-(CH2)x-CH3 (III alpha ) or ss) -CO-(CH2)y-CH=CH-(CH2)z-CH3 (IIIss), where x, y and z are each an integer, and x is in the range from 6 to 18, y is in the range from 1 to 16, z is in the range from 1 to 16 and y + z is in the range from 4 to 17, and c) a polyamine obtainable by reacting epichlorohydrin with an aliphatic primary monoamine or an N-alkylalkylenediamine of the formula (IV> R NH-R -NH2 (IV), where R is a C8-C24-alkyl radical and R is a C2-C6-alkylene radical. d

    17.
    发明专利
    未知

    公开(公告)号:ES2140579T3

    公开(公告)日:2000-03-01

    申请号:ES95108696

    申请日:1995-06-07

    Applicant: BASF AG

    Abstract: A catalyst system (I) for the polymerisation of olefinic hydrocarbons contains (A) a metal-amidinato complex of formula (A) and opt. (B) an acceptor cpd. for substit. X in (A) as activator; M = Sub-Gp. III, IV, V or VI metal or lanthanide metal; X = negative leaving atom or gp. (these can be identical or different if (n = m) is greater than 1); R -R = C-organic or Si-organic gps.; n = valency of M in complex (A); m = 1-5; n - m = O or more. Also claimed is a process for the prodn. of homo- or copolymers of ethylene and other olefins by insertion polymerisation using catalyst (I). Also claimed are polymers of ethylene and alkyl- and aryl-substd. olefins obtd. by this process.

    18.
    发明专利
    未知

    公开(公告)号:ES2096823T3

    公开(公告)日:1997-03-16

    申请号:ES93114892

    申请日:1993-09-16

    Applicant: BASF AG

    Abstract: Process for the preparation of a supported catalyst for the polymerisation of alpha -olefins, in which (1) a support gel containing silicon dioxide is prepared by (1.1) introducing a sodium or potassium waterglass solution into a rotating stream of an aqueous mineral acid both longitudinally and tangentially to the stream, spraying the silicic acid hydrosol thus formed in droplet form into a gaseous medium, allowing it to solidify into a hydrogel and freeing the hydrogel thus obtained of salt by washing without prior aging, (1.2) drying the hydrogel resulting from (1.1) to form the support gel, and (2) the support gel (1) is loaded with chromium trioxide or a chromium compound which can be converted into chromium trioxide under the conditions of the process step (3), which results in a chromium-containing support gel, and (3) the chromium-containing support gel (2) is heated in an anhydrous gas stream containing oxygen in a concentration of over 10% by volume for from 10 to 1000 minutes at from 400 to 1100 DEG C, the hydrogel resulting from the process step (1.1) being dried in the process step (1.2) over a time of not more than 60 seconds in a shaping flash dryer at an inlet temperature of from 80 to 400 DEG C .

    19.
    发明专利
    未知

    公开(公告)号:DE59305319D1

    公开(公告)日:1997-03-13

    申请号:DE59305319

    申请日:1993-09-16

    Applicant: BASF AG

    Abstract: Process for the preparation of a supported catalyst for the polymerisation of alpha -olefins, in which (1) a support gel containing silicon dioxide is prepared by (1.1) introducing a sodium or potassium waterglass solution into a rotating stream of an aqueous mineral acid both longitudinally and tangentially to the stream, spraying the silicic acid hydrosol thus formed in droplet form into a gaseous medium, allowing it to solidify into a hydrogel and freeing the hydrogel thus obtained of salt by washing without prior aging, (1.2) drying the hydrogel resulting from (1.1) to form the support gel, and (2) the support gel (1) is loaded with chromium trioxide or a chromium compound which can be converted into chromium trioxide under the conditions of the process step (3), which results in a chromium-containing support gel, and (3) the chromium-containing support gel (2) is heated in an anhydrous gas stream containing oxygen in a concentration of over 10% by volume for from 10 to 1000 minutes at from 400 to 1100 DEG C, the hydrogel resulting from the process step (1.1) being dried in the process step (1.2) over a time of not more than 60 seconds in a shaping flash dryer at an inlet temperature of from 80 to 400 DEG C .

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