Polyamides
    83.
    发明专利

    公开(公告)号:CZ20031428A3

    公开(公告)日:2003-10-15

    申请号:CZ20031428

    申请日:2001-11-22

    Applicant: BASF AG

    Abstract: A process for preparing polyamides comprises polymerizing starting monomers in the presence of from 2.3 to 10 mmol, based on 1 mol of carboxamide group of the polyamide, of a chain regulator containing a nitrile group and a functional group capable of forming a carboxamide group.

    84.
    发明专利
    未知

    公开(公告)号:BR0115543A

    公开(公告)日:2003-09-09

    申请号:BR0115543

    申请日:2001-11-22

    Applicant: BASF AG

    Abstract: A process for preparing polyamides comprises polymerizing starting monomers in the presence of from 2.3 to 10 mmol, based on 1 mol of carboxamide group of the polyamide, of a chain regulator containing a nitrile group and a functional group capable of forming a carboxamide group.

    85.
    发明专利
    未知

    公开(公告)号:BR0110452A

    公开(公告)日:2003-03-11

    申请号:BR0110452

    申请日:2001-04-30

    Applicant: BASF AG

    Abstract: A process for preparing a polymer, which comprisesa) reacting a mixture (I) containing 6-aminocapronitrile and water in the presence of a catalyst to obtain a mixture (II) containing caprolactam, ammonia, water, high boilers and low boilers, thenb) removing ammonia from mixture (II) to obtain a mixture (III) containing caprolactam, water, high boilers and low boilers, thenc) removing all or some of the water from mixture (III) to obtain a mixture (IV) containing caprolactam, high boilers and low boilers and thend) feeding mixture (IV) to a polymerization reaction, and also the polymer obtainable by this process, the use of the polymer for producing fibers, sheetlike structures and moldings, and also fibers, sheetlike structures and moldings obtainable using such a polymer.

    86.
    发明专利
    未知

    公开(公告)号:DE10058292A1

    公开(公告)日:2002-05-29

    申请号:DE10058292

    申请日:2000-11-23

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing polyamides. Said method is characterised in that the polymerisation of starting monomers is carried out in the presence of between 2.3 and 10 mmol - in relation to 1 mol of carboxamide group of the polyamide - of a compound used as a chain transfer agent, comprising a nitrile group and a functional group capable of forming a carboxamide group.

    Continuous polyamide production comprises a three-stage reaction of an amino nitrile with water and utilizes an organic diluent to reduce branching

    公开(公告)号:DE10033544A1

    公开(公告)日:2002-01-24

    申请号:DE10033544

    申请日:2000-07-11

    Applicant: BASF AG

    Abstract: Continuous polyamide production by three-stage reaction of an amino nitrile with water using a zeolite beta, layered silicate or titanium dioxide catalyst comprises performing the first stage in the presence of an organic liquid diluent. Continuous polyamide production comprises: (a) reacting at least one amino nitrile with water in the presence of an organic liquid diluent at 90-400 deg C and 0.1-35 MPa in a tubular reactor containing a Bronsted acid catalyst (I) selected from zeolite beta, layered silicates and titanium dioxide comprising 70-100 wt.% anatase and 0-30 wt.% rutile, in which up to 40 wt.% of the titanium dioxide can be replaced with tungsten oxide; (b) further reacting the product from (a) at 150-400 deg C and a pressure lower than that in step (a) in the presence of a catalyst of type (I) to form a gas phase and a liquid, solid or slurry phase, and separating the gas phase; and (c) contacting the liquid, solid or slurry phase with a water-containing gas or liquid phase at 150-370 deg C and 0.1-30 MPa. An Independent claim is also included for the polyamide produced by the process.

    88.
    发明专利
    未知

    公开(公告)号:DE19962573A1

    公开(公告)日:2001-07-05

    申请号:DE19962573

    申请日:1999-12-23

    Applicant: BASF AG

    Abstract: The invention relates to a method for the production of polyamides from amino nitriles and water, (1) by reacting aminonitriles with water at a temperature of 180 - 350 DEG C and a pressure of 30 - 120 bar adjusted in such a way that in addition to a liquid phase, a gaseous phase is also present in the first reaction step; (2) relaxation of the reaction mixture obtained in the first reaction step via an evaporator zone or adiabatically with removal of water and ammonia in a second reaction step and (3) post-condensation in the second reaction step at a pressure 0.1 mbar to 5 bar at a temperature of 230 - 320 DEG C.

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