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    2.
    发明专利
    未知

    公开(公告)号：DE50000852D1

    公开(公告)日：2003-01-16

    申请号：DE50000852

    申请日：2000-02-05

    Applicant: BASF AG

    Inventor： SANDER DR ,  PEISKER DIETMAR ,  WERNER KLAUS ,  BRAUNSBERG HOLGER ,  GEORGI DR ,  PENZEL DR

    IPC: B01J35/02 ,  B01J21/06 ,  B01J23/755 ,  B01J35/10 ,  C07B61/00 ,  C07C209/36 ,  C07C211/50

    Abstract: Production of amines (I) by hydrogenating at least one nitro compound (II) in presence of a supported catalyst (A) that contains nickel as catalytically active metal, optionally together with at least one metal of subgroups I, V, VI and/or VIII. The reduced and stabilized catalyst contains nickel crystallites with a bimodal distribution of size, with maxima at 30-80 and 81-150 Angstrom , and after reduction at 100 degrees C has a degree of reduction at least 70%. The support is one or more of zirconia, hafnia and/or silica and the reduced and passivated catalyst contains, by weight, 60-80% nickel; 0-20% silica; 0-40% zirconia and 0-4% hafnia.

    3.
    发明专利
    未知

    公开(公告)号：DE59911344D1

    公开(公告)日：2005-01-27

    申请号：DE59911344

    申请日：1999-01-26

    Applicant: BASF AG

    Inventor： STROEFER DR ,  JACOBS JAN D ,  SEYFERT DR ,  SCHWARZ DR ,  SCHWEERS DR ,  SCHARR VOLKER ,  PENZEL DR

    IPC: C07B61/00 ,  C07C209/78 ,  C07C211/45 ,  C07C211/50 ,  C07C263/10 ,  C07C265/14

    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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