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公开(公告)号：SG11202100565TA
公开(公告)日：2021-02-25
申请号：SG11202100565T
申请日：2019-07-24
Applicant: BASF SE
Inventor： OLBERT GERHARD , PASIN E MATOS LAILA RAQUEL
Abstract: The present invention is directed to hollow aluminosilicate glass particles and a process for the production thereof. Further, the present invention is directed to an article comprising said hollow aluminosilicate glass particles as well as the use of said particles as a filler for high temperature products, molten metal, injection moulded synthetic materials, flame-retardant insulating foams, cement slurries, mortars, concretes and oil field applications.
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公开(公告)号：AU2019316684A1
公开(公告)日：2021-02-25
申请号：AU2019316684
申请日：2019-08-05
Applicant: BASF SE
Inventor： KOLIOS GRIGORIOS , ZOELS BERND , APPEL HAGEN , BERNNAT JENS , GLENK FRIEDRICH , FLICK DIETER , OLBERT GERHARD , SCHEIFF FREDERIK , ANDERLOHR CHRISTOPHER ALEC
Abstract: The present invention relates to a device comprising at least one pressure-bearing device shell and at least one modular scaffolding system made of ceramic fibre composite materials and arranged inside the device shell and a modular lining device comprising refractory bricks in addition to the modular scaffolding system, and to the use of this device for high-temperature reactors, in particular electrically heated high-temperature reactors.
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公开(公告)号：AU2019309025A1
公开(公告)日：2021-02-11
申请号：AU2019309025
申请日：2019-07-24
Applicant: BASF SE
Inventor： OLBERT GERHARD , PASIN E MATOS LAILA RAQUEL
Abstract: The present invention is directed to hollow aluminosilicate glass particles and a process for the production thereof. Further, the present invention is directed to an article comprising said hollow aluminosilicate glass particles as well as the use of said particles as a filler for high temperature products, molten metal, injection moulded synthetic materials, flame-retardant insulating foams, cement slurries, mortars, concretes and oil field applications.
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公开(公告)号：CA3105264A1
公开(公告)日：2020-01-30
申请号：CA3105264
申请日：2019-07-24
Applicant: BASF SE
Inventor： OLBERT GERHARD , PASIN E MATOS LAILA RAQUEL
Abstract: The present invention is directed to hollow aluminosilicate glass particles and a process for the production thereof. Further, the present invention is directed to an article comprising said hollow aluminosilicate glass particles as well as the use of said particles as a filler for high temperature products, molten metal, injection moulded synthetic materials, flame-retardant insulating foams, cement slurries, mortars, concretes and oil field applications.
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Patent Agency Ranking
公开(公告)号：HUE031742T2
公开(公告)日：2017-07-28
申请号：HUE12743169
申请日：2012-08-02
Applicant: BASF SE
Inventor： MATTKE TORSTEN , OLBERT GERHARD
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公开(公告)号：ES2385380T3
公开(公告)日：2012-07-24
申请号：ES06794009
申请日：2006-10-11
Applicant: BASF SE , STYROLUTION GMBH
Inventor： CHENG TSUNG-CHIEH , OLBERT GERHARD , SCHMAUS PAULUS , WASSMER KARL-HEINZ , SAUER MICHAEL , BARDON RAINER , CZAUDERNA BERNHARD
Abstract: Intercambiador de calor de haz de tubos (R) para eliminar sustancias disueltas a partir de una disolución depolímero (4) mediante desgasificación, con un haz de tubos (1) dispuestos en paralelo entre sí y en vertical, queestán sujetos a ambos extremos en cada caso en una plataforma de tubos (2), y circulando por los tubos (1) ladisolución de polímero (4), así como con un espacio de revestimiento (5) alrededor de los tubos (1), por el quecircula un portador de calor líquido (6), con chapas de desviación (7) en el espacio de revestimiento (5), que estándispuestas en cada caso en planos de sección transversal del intercambiador de calor de haz de tubos (R) y en cadacaso liberan una zona de desviación (8) para el portador de calor (6), no estando dispuesto en las zonas dedesviación (8) ningún tubo (1); caracterizado por que está dispuesta una estructura interna en cada tubo (1), queestrecha la sección transversal de paso libre a través del tubo, y por que todas las estructuras internas (3) tienen unaconstrucción idéntica, así como por que las estructuras internas (3) están fijadas mediante una unión roscada en laplataforma de tubos (2) y por que los puntos de soldadura de los tubos (1) se encuentran por debajo de la uniónroscada para las estructuras internas (3), y por que las estructuras internas (3) presentan una abertura central, queatraviesa las estructuras internas (3), que puede usarse para insertar una llave poligonal para enroscar lasestructuras internas en la plataforma de tubos (2) con una llave poligonal y tras retirar la llave poligonal paraalimentar la disolución de polímero (4).
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67.发明专利
公开(公告)号：ZA201102538B
公开(公告)日：2012-06-27
申请号：ZA201102538
申请日：2011-04-06
Applicant: BASF SE
Inventor： OLBERT GERHARD , BIHL RALF
IPC: B01J20060101
Abstract: What is proposed is an apparatus for automatic catalyst exchange in a plurality of process steps in the catalyst tubes of a reactor with a bundle of catalyst tubes, which are welded in or rolled in between an upper tube plate and a lower tube plate in longitudinal direction of the reactor, and welded tight, comprising a tool carrier device, which is arranged so as to be mobile in a plane above and parallel to the upper tube plate, and which can be equipped with an exchangeable tool for each process step, the exchangeable tool being mobile together with the tool carrier device in the plane above and parallel to the upper tube plate and also vertically, in the direction of the longitudinal axis of the reactor, and being able to access each individual catalyst tube with control by means of a control unit, the position of the longitudinal axis of each individual catalyst tube being measured or calculated and recorded in the control unit in a position database.
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公开(公告)号：ZA200904965B
公开(公告)日：2010-09-29
申请号：ZA200904965
申请日：2009-07-16
Applicant: BASF SE
Inventor： OLBERT GERHARD , CRONE SVEN , CORR FRANZ
IPC: B01F20060101 , B01J20060101
Abstract: A reactor (1) for carrying out a reaction between two fluid starting materials (2, 3) over a catalyst bed (4) with premixing of the fluid starting materials before introduction into the catalyst bed within a delay time of less than 150 minutes comprises a mixing-in device (5) containing transversally arranged to the inflow direction of the first fluid starting material stream, two/three rows arranged behind one another of tubes which have turbulence generators on the outside, a perforated plate upstream of the tubes and a perforated plate downstream of the tubes. A reactor (1) for carrying out a reaction between two fluid starting materials (2, 3) over a catalyst bed (4) with premixing of the fluid starting materials before introduction into the catalyst bed within a delay time of less than 150 minutes comprises a mixing-in device (5) containing transversally arranged to the inflow direction of the first fluid stream, two/three rows of tubes arranged behind one another and having turbulence generators on the outside, and constrict the flow cross section for the first fluid starting material stream to from 1/2 to 1/10, with the second fluid starting material stream being passed through the interiors of the tubes and injected via openings in the tubes into the first fluid starting material stream; a perforated plate upstream of the tubes; and a perforated plate downstream of the tubes. Independent claims are included for the following (1) mixing-in device for the reactor; and (2) static mixer for at least two fluid composed of the elements of the mixing-in device.
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公开(公告)号：ES2336469T3
公开(公告)日：2010-04-13
申请号：ES05819946
申请日：2005-12-21
Applicant: BASF SE
Inventor： HECHLER CLAUS , OLBERT GERHARD
IPC: C07C51/265 , C07D307/89
Abstract: Procedimiento para la obtención de anhídrido de ácido ftálico a través de la oxidación parcial catalítica de o-xileno y/o naftalina con un gas que contiene oxígeno en una instalación con - dos o más zonas de reacción refrigeradas con un medio refrigerante, - uno o más dispositivos dispuestos entre las zonas de reacción, para la refrigeración intermedia de la mezcla de reacción entre las zonas de reacción, en el cual, la temperatura del medio refrigerante se reduce al entrar en la segunda o en otra zona de reacción, en relación a la temperatura del medio refrigerante al entrar en la primera zona de reacción, caracterizado porque la temperatura del medio refrigerante es más de 20º mayor al entrar en la primera zona de reacción que la temperatura del medio refrigerante al entrar en la segunda o en otra de las zonas de reacción.
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