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公开(公告)号:CA1211889A
公开(公告)日:1986-09-23
申请号:CA447878
申请日:1984-02-21
Applicant: BASF AG
Inventor: PIPPER GUNTER , THEYSOHN RAINER , ZAHRADNIK FRANZ
Abstract: - 8 - O.Z. 0050/36394 Polylactams are prepared continuously by a process in which a lactam containing from 1 to 25% by weight of water is heated in a prepolymerization zone under a pressure of from 1 to 10 bar at from 220 to 280.degree.C for from 1 to 10 minutes, water being vaporized at the same time, with the proviso that the degree of conversion on emergence from the prepolymerization zone is not Less than 85%, the prepolymer and the vapor are separated continuously, and the prepolymer is passed into a polymerization zone and is polymerized further under superatmospheric pressure at from 240 to 290.degree.C.
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公开(公告)号:FI70240C
公开(公告)日:1986-09-15
申请号:FI810481
申请日:1981-02-17
Applicant: BASF AG
Inventor: REIMANN HORST , SCHMIDT FRANZ , WEISS HANS-PETER , PIPPER GUNTER
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公开(公告)号:DE3330154A1
公开(公告)日:1985-03-07
申请号:DE3330154
申请日:1983-08-20
Applicant: BASF AG
Inventor: BLINNE GERD DR , PIPPER GUNTER , STEGMAIER WOLFGANG DR
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公开(公告)号:DE3321581A1
公开(公告)日:1984-12-20
申请号:DE3321581
申请日:1983-06-15
Applicant: BASF AG
Inventor: SCHMIDT FRANZ DR , PIPPER GUNTER , FLOSS JOSEF GEORG DR , ZAHRADNIK FRANZ DR
Abstract: Nylons are prepared by a continuous process in which, in an evaporator zone, an aqueous solution of a salt of a dicarboxylic acid of 6 to 18 carbon atoms and a diamine of 6 to 18 carbon atoms is heated to 250 DEG -300 DEG C. under superatmospheric pressure, with simultaneous vaporization of water and formation of a prepolymer, the prepolymer and the vapors are separated continuously, the vapors are rectified and the entrained diamines are recycled, and the prepolymer is fed to a polycondensation zone and subjected to polycondensation under superatmospheric pressure of from 1 to 10 bar and at from 250 DEG to 300 DEG C., wherein the aqueous salt solution is heated under superatmospheric pressure of from 1 to 10 bar during a residence time of less than 60 seconds, with the proviso that, on leaving the evaporator zone, the degree of conversion is not less than 93% and the water content of the prepolymer is not more than 7% by weight.
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