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    Reactor with a bunch of heat-exchange tubes
    71.
    发明专利
    Reactor with a bunch of heat-exchange tubes 未知

    公开(公告)号：CZ2001524A3

    公开(公告)日：2001-07-11

    申请号：CZ2001524

    申请日：1999-08-06

    Applicant: BASF AG

    Inventor： CORR FRANZ ,  OLBERT GERHARD

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/27 ,  C07C47/127 ,  C07C51/16 ,  C07C51/25 ,  C07C51/255 ,  C07C57/04 ,  C07C57/05 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14 ,  F28D7/16 ,  F28F9/02 ,  F28F9/22 ,  F28F27/02

    Abstract: The invention proposes a reactor (1) having a contact tube bundle (2) through whose space surrounding the contact tubes a heat-exchange medium circuit is passed, with ring lines (3, 4) at both ends of the reactor with jacket apertures (5, 6) for the supply and discharge of a heat-exchange medium by means of a pump via an external heat exchanger, where the heat-exchange medium is fed to the lower ring line (4) and is discharged to the heat exchanger via the upper ring line (3), and with baffle plates (7) which leave a passage cross section alternately in the reactor center and at the reactor edge. The upper (3) and lower (4) ring lines are each divided into an inner (11, 13) and an outer (12, 14) ring line by a cylindrical partition wall (8, 9), and the heat-exchange medium is fed to the outer lower ring line (14), via a region outside the reactor to the inner upper ring line (11), via the jacket apertures (5) of the latter to the region surrounding the contact tubes (2), via the jacket apertures (6) to the inner lower ring line (13) and subsequently via a region outside the reactor to the outer upper ring line (12).

    72.
    发明专利
    未知

    公开(公告)号：BR9912930A

    公开(公告)日：2001-05-08

    申请号：BR9912930

    申请日：1999-08-06

    Applicant: BASF AG

    Inventor： CORR FRANZ ,  OLBERT GERHARD

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/27 ,  C07C47/127 ,  C07C51/16 ,  C07C51/25 ,  C07C51/255 ,  C07C57/04 ,  C07C57/05 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14 ,  F28D7/16 ,  F28F9/02 ,  F28F9/22 ,  F28F27/02

    Abstract: The invention proposes a reactor (1) having a contact tube bundle (2) through whose space surrounding the contact tubes a heat-exchange medium circuit is passed, with ring lines (3, 4) at both ends of the reactor with jacket apertures (5, 6) for the supply and discharge of a heat-exchange medium by means of a pump via an external heat exchanger, where the heat-exchange medium is fed to the lower ring line (4) and is discharged to the heat exchanger via the upper ring line (3), and with baffle plates (7) which leave a passage cross section alternately in the reactor center and at the reactor edge. The upper (3) and lower (4) ring lines are each divided into an inner (11, 13) and an outer (12, 14) ring line by a cylindrical partition wall (8, 9), and the heat-exchange medium is fed to the outer lower ring line (14), via a region outside the reactor to the inner upper ring line (11), via the jacket apertures (5) of the latter to the region surrounding the contact tubes (2), via the jacket apertures (6) to the inner lower ring line (13) and subsequently via a region outside the reactor to the outer upper ring line (12).

    Multi-tube fixed-bed reactor, especially for catalytic gas phase reactions
    73.
    发明专利
    Multi-tube fixed-bed reactor, especially for catalytic gas phase reactions 未知

    公开(公告)号：AU4538700A

    公开(公告)日：2000-10-04

    申请号：AU4538700

    申请日：2000-03-15

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  CORR FRANZ ,  REUTER PETER ,  WAMBACH LUDWIG ,  HAMMON ULRICH

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C45/38 ,  H01Q21/08 ,  B01J8/00

    Abstract: A multitube fixed bed reactor and the use of such a reactor for carrying out catalytic gas-phase reactions, in particular for carrying out exothermic and endothermic catalytic gas-phase reactions such as the preparation of phthalic anhydride (PA), acrylic acid, methacrylic acid (MAA), acrolein, maleic anhydride (MA), glyoxal, phosgene, hydrocyanic acid or vinyl formamide (VFA). In a relatively large multitube reactor in which a large amount of heat of reaction is generated owing to the numerous catalyst tubes ( 17 ) and has to be removed, it is proposed that the ratio of tube spacing t to external tube diameter d a be made dependent on the reactor diameter or on the external tube bundle diameter d RBa . At an external diameter of the catalyst tube bundle ( 18 ) of more than 4 meters, a ratio of tube spacing d to external tube diameter d a of at least 1.3 is preferred.

    REACTOR FOR PARTIAL OXIDATION WITH HEAT-TRANSFER SHEET MODULES
    76.
    发明专利
    REACTOR FOR PARTIAL OXIDATION WITH HEAT-TRANSFER SHEET MODULES 未知

    公开(公告)号：CA2532646C

    公开(公告)日：2012-09-11

    申请号：CA2532646

    申请日：2004-07-21

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  HECHLER CLAUS

    IPC: B01J19/32 ,  B01J19/24 ,  C07C45/35 ,  C07C51/215 ,  C07C51/25 ,  C07C57/04 ,  F28D9/00 ,  F28F9/00

    Abstract: The invention relates to a reactor for partial oxidation of a fluid reaction mixture in the presence of a heterogeneous particulate catalyst. Said reactor comprises one or several cuboid heat-transfer sheet modules (1) which are each composed of two or several right-angled heat-transfer sheets (2), arranged parallel to each other such as to form a slit (3) which can be filled with the heterogeneous particulate catalyst and through which the fluid reaction mixture flows, the heat of reaction being absorbed by a heat carrier which flows through the heat-transfer sheets (2) and at least partially evaporates. Said reactor also comprises a mainly cylindrical envelope (4, 15, 16) which depressurizes the heat-transfer sheet modules and fully surrounds said modules, said envelope being composed of a cylinder casing (4) and of caps (15, 16), closing said casing at both ends, the longitudinal axis of which extends parallel to the plane of said heat-transfer sheets (2). Said reactor finally comprises one or several sealing elements (7, 23), arranged so that the fluid reaction mixture flows only through the slit (3), except through the reactor interior spaces, defined by the caps (15, 16).

    PROCEDIMIENTO PARA LA PRODUCCION DE CLORO MEDIANTE LA OXIDACION EN FASE GASEOSA DE CLORURO DE HIDROGENO.
    79.
    发明专利
    PROCEDIMIENTO PARA LA PRODUCCION DE CLORO MEDIANTE LA OXIDACION EN FASE GASEOSA DE CLORURO DE HIDROGENO. 未知

    公开(公告)号：ES2268471T3

    公开(公告)日：2007-03-16

    申请号：ES03789224

    申请日：2003-12-11

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  WALSDORFF CHRISTIAN ,  HARTH KLAUS ,  STROFER ECKHARD ,  FIENE MARTIN

    IPC: C01B7/04 ,  B01J8/00 ,  B01J8/06

    Abstract: Procedimiento para la producción de cloro mediante la oxidación en fase gaseosa de cloruro de hidrógeno con un flujo de gas que contiene oxígeno molecular en presencia de un catalizador de lecho fijo, caracterizado porque se realiza el procedimiento en un reactor (1) con un haz de tubos (2) de contacto dispuestos paralelos entre sí en la dirección longitudinal del reactor, que están fijados en sus extremos a fondos (3) de tubos, con en cada caso una cubierta (4) en ambos extremos del reactor (1), así como con una o varias planchas (6) de desvío dispuestas verticales con respecto a la dirección longitudinal del reactor en el espacio (5) entre los tubos (2) de contacto, que dejan abiertos de manera alternante orificios (7) de paso enfrentados entre sí en la pared interna del reactor (1), estando los tubos (2) de contacto rellenos con el catalizador de lecho fijo, conduciéndose el flujo de gas que contiene el cloruro de hidrógeno así como el oxígeno molecular desde un extremo del reactor sobreuna cubierta (4) mediante los tubos (2) de contacto y extrayéndose la mezcla de reacción gaseosa desde el extremo del reactor opuesto sobre la segunda cubierta (4) y conduciéndose por el espacio (5) alrededor de los tubos (2) de contacto un medio de intercambio de calor líquido.

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