181.
    发明专利
    未知

    公开(公告)号:DE19731230A1

    公开(公告)日:1999-01-28

    申请号:DE19731230

    申请日:1997-07-21

    Applicant: BASF AG

    Abstract: A moulding composition comprising: (a) 5-95 wt.% random copolyamide (I) of (a1) 95.1-99.9 wt.% component (IA) of equimolar amounts of linear aliphatic diamine(s) and linear aliphatic dicarboxylic acid(s) and (a2) 0.1-4.9 wt.% component (IB) of equimolar amounts of linear aliphatic diamine(s) and isophthalic acid; and (b) 5-95 wt.% other copolymer (II), selected from (b1) optionally modified polyarylene ether(s) (IIA), (b2) component (IIB) a mixture of 60-99 wt.% (co)polyolefin(s) (IIB.1) and 1-40 wt.% modified (co)polyolefin(s) (IIB.2) or (b3) a component (IIC) comprising 70-100 wt.% styrene-acrylonitrile (SAN), acrylonitrile-butadiene-styrene (ABS) and/or acrylonitrile-styrene-acrylic ester (ASA) polymer(s) (IIC.1) and 0-30 wt.% modified SAN, ABS or ASA polymer(s) (IIC.2). The composition may also contain: (c) 0-20 wt.% impact modifier(s), (d) 0-50 wt.% filler(s) and (e) 0-20 wt.% usual additives. Also claimed are: (i) a method of producing the composition; and (ii) mouldings, fibers, or films produced from the composition.

    Continuous preparation of poly:amide(s) from omega-amino:alkyl nitrile and water

    公开(公告)号:DE19635077A1

    公开(公告)日:1998-03-05

    申请号:DE19635077

    申请日:1996-08-30

    Applicant: BASF AG

    Abstract: A continuous multi-step process for the preparation of polyamides by reacting an w-aminoalkyl nitrile with water at high temperature and pressure, comprises (1) heating an w-aminoalkyl nitrile in an excess amount of water at 250-350 deg C and 4-30 MPa, the temperature and pressure being chosen to give a single-phase liquid reaction mixture, in which at least 95 mol.% nitrile groups are converted to form a first reaction product (I); (2) heating (I) at 220-300 deg C and 1-7 MPa, so that the pressure is at least 0.5 MPa less than that in step (1), whilst separating the gas and liquid phases to form a second reaction product (II); (3) heating (II) at 220-300 deg C and 10-300 kPa in a first sub-step (3a), then in a second sub-step (3b) the gas phase is separated from the liquid phase and then in a third sub-step (c) the relative viscosity (measured at 25 deg C and a concentration of 1 g polymer per 100 ml sulphuric acid (96 wt.%)) of the polyamide is altered to a value of 1.6-3.5 by selecting the appropriate temperature and dwell time, whilst in the final sub-step (3d) the third reaction product (III) is isolated by standard techniques and optionally processed.

    187.
    发明专利
    未知

    公开(公告)号:NO973767D0

    公开(公告)日:1997-08-15

    申请号:NO973767

    申请日:1997-08-15

    Applicant: BASF AG

    Abstract: PCT No. PCT/EP96/00458 Sec. 371 Date Aug. 14, 1997 Sec. 102(e) Date Aug. 14, 1997 PCT Filed Feb. 3, 1996 PCT Pub. No. WO96/25448 PCT Pub. Date Aug. 22, 1996Biodegradable polymers comprising a polyether ester P1 obtained by reacting a first mixture of 20-95 mol% of adipic acid or ester-forming derivatives thereof or mixtures thereof, 5-80 mol% of terephthalic acid or ester-forming derivatives thereof or mixtures thereof, and 0-5 mol% of a compound containing sulfonate groups, and a second mixture of 15-99.8 mol% of a dihydroxy compound selected from the group consisting of C2-C6-alkanediols and C5-C10-cycloalkanediols, 85-0.2 mol% of a dihydroxy compound IHO-[(CH2)n-O]m-H(n=2, 3 or 4, m=2-250) with 0-5 mol%, based on the first mixture, of a compound D having at least three groups capable of ester formation, and a bisoxazoline C1, their preparation and their use in the manufacture of biodegradable molding materials.

    Process for the continuous production of low molecular polyamides

    公开(公告)号:AU7186594A

    公开(公告)日:1995-01-24

    申请号:AU7186594

    申请日:1994-06-20

    Applicant: BASF AG

    Abstract: PCT No. PCT/EP94/01998 Sec. 371 Date Dec. 28, 1995 Sec. 102(e) Date Dec. 28, 1995 PCT Filed Jun. 20, 1994 PCT Pub. No. WO95/01389 PCT Pub. Date Jan. 12, 1995A process for the continuous production of polyamides from a mixture of at least one lactam and water and, if required, other monomer units and/or conventional additives and fillers under polyamide-forming conditions, where the mixture of the starting materials is heated in liquid phase in a first reaction zone until a conversion of at least 70% is reached, and undergoes adiabatic decompression and further polymerization in another reaction zone, wherein, in the first reaction zone, 0.5-7% by weight of water are employed, the temperature is increased to the range from 220 DEG to 310 DEG C., and polymerization is carried out until a conversion of at least 85% is reached and, in the second reaction zone, after the decompression further polymerization is carried out in the range from 215 DEG to 300 DEG C. without heat input.

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