2.
    发明专利
    未知

    公开(公告)号:DE3638218A1

    公开(公告)日:1988-05-11

    申请号:DE3638218

    申请日:1986-11-08

    Applicant: BASF AG

    Abstract: A method for the continuous production of alkyl esters of pentenric acid by reacting butadiene-containing C4 sections with alkanols and carbon monoxide in the presence of cobalt carbonyl catalysts and heterocyclic aromatic tertiary nitrogen bases at a temperature of 100 to 160 DEG C and under a pressure of 100 to 1200 bar, characterised in that the reaction mixture is passed essentially without remixing through a treatment zone at the rate at which it is formed at a temperature of 100 to 160 DEG C under a pressure of 250 to 1200 bar and with a residence time of 10 to 60 minutes.

    5.
    发明专利
    未知

    公开(公告)号:DE19804915A1

    公开(公告)日:1999-08-12

    申请号:DE19804915

    申请日:1998-02-07

    Applicant: BASF AG

    Abstract: The invention relates to a method for the production of methylenedi(phenylamine) by reacting aniline with formaldehyde in the presence of acid catalysts. The method is characterized in that aniline and optionally an acid catalyst are treated in a semi-continuos method; formaldehyde and optionally an acid catalyst are fed through a mixing organ in a circuit in which aniline, optionally an acid catalyst and optionally an already added formaldehyde are circulated and tempering the reaction mixture at a temperature of over 75 DEG C after feeding at least 50 % of the total amount of formaldehyde. The invention also relates to a method for the production of polyisocyanates by phosgenating the amines thus obtained and the polyisocyanates obtained according to this method.

    8.
    发明专利
    未知

    公开(公告)号:DE3774080D1

    公开(公告)日:1991-11-28

    申请号:DE3774080

    申请日:1987-11-23

    Applicant: BASF AG

    Abstract: Prodn. of butanedicarboxylic acid methyl esters (I) is effected by reacting a methyl pentenoate (II) with CO and MeOH in the presence of pyridine and/or picolines (III) and a Co catalyst at elevated temp. and pressure, and treating the reaction mixt. with an O2-contg. gas and aq. HOAc. (III) are recovered by (a) sepg. the reaction mixt. into an aq. phase contg. Co(OAc)2, (III), HOAc and MeOH, and an organic phase contg. (I), by-products, (II), HOAc and (III); (b) extracting (III) from the organic phase with aq. HOAc; (c) combining the extract with the aq. phase; and (d) distilling (III) from the mixt. to leave an aq. soln. contg. Co(OAc)2 and HOAc.

    9.
    发明专利
    未知

    公开(公告)号:PT1270544E

    公开(公告)日:2005-05-31

    申请号:PT02022029

    申请日:1999-01-26

    Applicant: BASF AG

    Abstract: The production of methylene-di-phenylamine from aniline (A) and formaldehyde (F) with an acid catalyst (C) comprises placing (A) and possibly (C) in a reactor, feeding (F) and possibly (C) through a mixer into a circulation loop containing (A), possibly (C) and possibly (F), and heating to above 75 degrees C after adding at least 50% of the total (F). Independent claims are also included for: (a) mixtures containing methylene-di-phenylamine (MDA) obtained by this process; (b) a process for the production of polyisocyanates by phosgenation of these mixtures; (c) a process for the production of methylene-diphenylisocyanate (MDI) by phosgenation of MDA (obtained as above) at 50-150 degrees C and 0.5-10 bar, optionally in presence of inert solvent; (d) a process for the production of MDI comprising: (1) the semi-continuous process described above using a mol ratio of (A):(C) = (1:0.6)-(1:0.01) and a mol ratio of (A):(total F) = (1.7:1)-(7.2:1), in which the temperature of the circulating mixture is 20-75 degrees C and the mixture is heated for at least 0.2 hour at above 75 degrees C after adding at least 50% of the (F), (2) neutralization, (3) distillation of water and aniline, (4) phosgenation of the purified MDA as in (c) above, (5) removal of phosgene, hydrogen chloride and possibly solvent at below 150 degrees C under vacuum or inert gas, (6) removal of solvent at not above 1900 degrees C and (7) isolation of 2,2'-, 2,4'- and/or 4,4'-MDI and/or mixtures of at least two of these isomers by distillation at 2-50 mbar and 150-250 degrees C and/or by crystallization; and (e) polyisocyanates obtained by these processes.

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