PRESSING METHOD FOR ETHYLENIC UNSATURATED MONOMER AND COMONOMER OBTAINED THEREBY

    公开(公告)号:JP2000191558A

    公开(公告)日:2000-07-11

    申请号:JP36153599

    申请日:1999-12-20

    Applicant: BASF AG

    Abstract: PROBLEM TO BE SOLVED: To perform a pressure application operation on ethylenic unsaturated monomer more effectively than a conventional method so that sediments formed through early polymerization during pressure application are decreased by applying pressure in the absence of a polymerization initiator and in the presence of a specific nitrosyl compound. SOLUTION: Pressure is applied on an ethylenic unsaturated monomer (suitably, a mixture consisting of ethylene, propylene, butene and/or butadiene; more suitable monomer/comonomer is acrylic acid and/or methacrylic acid or the like) at 200-5000 bar in the presence of a nitrosyl compound of the formula (R1 and R2 are each a 1-4C alkyl or they form a 5-6 membered unsaturated hydrocarbon ring together with carbon atom(s) bound to them; R3 is a 1-4C alky; and R4 is H or a 1-12C alkyl) and in the absence of a polymerization initiator. The final pressure is preferably 1000-4000 bar, and a pressing temperature is preferably 20-140 deg.C. The compound of the formula is used preferably in an amount of 0.00001-1 wt.% based on the amount of the monomer to be pressed.

    PRODUCTION OF OXIDIZED POLYOLEFIN WAX

    公开(公告)号:JPH10279624A

    公开(公告)日:1998-10-20

    申请号:JP440198

    申请日:1998-01-13

    Applicant: BASF AG

    Abstract: PROBLEM TO BE SOLVED: To obtain an oxidized polyolefin wax having a narrow acid value distribution continuously in a high time and space yield by continuously reacting a polyolefin wax with oxygen or an oxygen-contg. gas in a tubular reactor at specified temp. and pressure (provided the reaction of a polyolefin obtd. with a metallocene catalyst is excluded). SOLUTION: A polyolefin wax is reacted at 140-200 deg.C under 5-200 bar. The use of air is pref. for oxidizing a polyolefin. Pref., at least two zones with temps. different from each other are established in the heating jacket of the tubular reactor, and the temp. of the preceding zone is set 5-20 deg.C higher than that of the following zone. The average dwell time is usually 0.5-20 hr. Pref., the ratio of flow rate of the oxidizing gas to the wax passing through the reactor is set at 30-500. Thus is obtd. an oxidized polyolefin wax having an acid value of 1-150.

    4.
    发明专利
    未知

    公开(公告)号:DE19754039A1

    公开(公告)日:1999-06-24

    申请号:DE19754039

    申请日:1997-12-05

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing ethylene/vinyl acetate copolymers in which a mixture comprised of ethylene and vinyl acetate is continuously polymerized in the presence of radical polymerization initiators and optional molecular weight modifiers in a cooled tubular reactor at a pressure ranging from 1000 to 3500 bar. The polymerization initiator is charged at the beginning and at a number of positions along the tubular reactor, and the temperature changes in the reaction mixture range no more than 20 C between the first maximum temperature and the last charging of the polymerization initiator along the tubular reactor.

    8.
    发明专利
    未知

    公开(公告)号:DE19700892A1

    公开(公告)日:1998-07-16

    申请号:DE19700892

    申请日:1997-01-14

    Applicant: BASF AG

    Abstract: A process for the production of oxidised polyolefin wax (I) comprises the continuous reaction of polyolefin wax (II) with oxygen or oxygen-containing gas at 140-200 degrees C and 5-200 bar in a tubular reactor, excluding polyolefins obtained by metallocene catalysis. Also claimed is oxidised polyolefin wax (I) obtained by this process, preferably with an acid number of 10-50.

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