HYDRODYNAMICALLY OPTIMIZED CATALYTIC STRUCTURE

    公开(公告)号:JP2001162178A

    公开(公告)日:2001-06-19

    申请号:JP2000312998

    申请日:2000-10-13

    Applicant: BASF AG

    Abstract: PROBLEM TO BE SOLVED: To provide a molded catalytic structure having a shape to uniformize the flow velocity of a gas passing through the inside of a catalyst and accordingly having a shape to prolong the service life of the catalyst because of its uniform thermal stress. SOLUTION: The molded catalytic structure has an upstream end face 3, a downstream end face 4 and a circumferential face 5. In this case, the upstream end face is formed in the shape of the side face 8 of a conical or truncated- conical protrusion 7, and the side face 8 has at least a concave curved surface.

    5.
    发明专利
    未知

    公开(公告)号:DE50305797D1

    公开(公告)日:2007-01-04

    申请号:DE50305797

    申请日:2003-12-16

    Applicant: BASF AG

    Abstract: Method for purifying isocyanates (I) by distillation. Method for purifying isocyanates by distillation comprises: (a) first separating a stream (1) containing (I), high and low boilers and non-evaporatable residue (X) by distillation (at least one theoretical plate) into a sidestream (2), containing (I) and (X), and a vapor stream (3), containing (I) and low boilers; (b) (X) in (2) is kept separate from (3) and/or material streams that consist at least partly of (3); (c) another (I)-containing vapor stream (4) is separated from (2), leaving stream (8) consisting essentially of (X); (d) streams (4) and (3) are separated by distillation into 3 streams (5,6,7) of different boiling ranges, where the lowest boiler (5) contains a significant proportion of the low boilers in (1), the highest boiler (7) contains a significant proportion of the high boilers in (1) and the middle stream (6) is essentially (I).

    9.
    发明专利
    未知

    公开(公告)号:DE102004030164A1

    公开(公告)日:2006-01-19

    申请号:DE102004030164

    申请日:2004-06-22

    Applicant: BASF AG

    Abstract: The invention relates to a process for preparing isocyanates by reacting amines with phosgene in the gas phase in a reaction zone, with the reaction mixture being passed through a zone into which a liquid is sprayed to stop the reaction, wherein the reaction mixture is passed through a zone having a reduced flow cross section between the reaction zone and the zone into which the liquid is sprayed.

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