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公开(公告)号：NZ547317A
公开(公告)日：2010-09-30
申请号：NZ54731704
申请日：2004-12-23
Applicant: BASF AG
Inventor： OLBERT GERHARD , JOHANN THORSTEN , WEBER MARKUS , LANG NEVEN , STROEFER ECKHARD , FIENE MARTIN , SIEGERT MARKUS
Abstract: A method for the production of formaldehyde by gas phase oxidation of methanol vapour with a gas flow containing a molecular oxygen in the presence of solid bed catalyst containing iron and molybdenum is carried out in a reactor (1) comprising thermal sheet metal plates (2) which are arranged in the longitudinal direction of the reactor (1) and spaced from each other. A heat transfer medium flows through the gaps between the plates. The heat transfer medium is transferred via inlets and outlets 3, 4 to the thermal sheet steel plates (2), and gaps (5) between the thermal sheet steel metal plates (2) and which are filled with the solid bed catalyst and into which the gas containing the methanol vapour and the molecular oxygen flows.
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公开(公告)号：BRPI0417455A
公开(公告)日：2007-05-22
申请号：BRPI0417455
申请日：2004-12-23
Applicant: BASF AG
Inventor： OLBERT GERHARD , JOHANN THORSTEN , WEBER MARKUS , LANG NEVEN , FER ECKARD STR , FIENE MARTIN , SIEGERT MARKUS
Abstract: A process for preparing formaldehyde by gas-phase oxidation of methanol vapor by means of a gas stream comprising molecular oxygen in the presence of a fixed-bed catalyst comprising iron and molybdenum, wherein the process is carried out in a reactor ( 1 ) having heat-exchange plates ( 2 ) which are arranged in the longitudinal direction of the reactor ( 1 ) and have a spacing between them and through which a heat transfer medium flows, inlet and outlet facilities ( 3, 4 ) for the heat transfer medium to the heat-exchange plates ( 2 ) and also gaps ( 5 ) between heat-exchange plates ( 2 ) in which the fixed-bed catalyst is present and into which the methanol vapor and the gas stream comprising molecular oxygen are passed, is described.
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公开(公告)号：BRPI0412785A
公开(公告)日：2006-09-26
申请号：BRPI0412785
申请日：2004-07-21
Applicant: BASF AG
Inventor： OLBERT GERHARD , HECHLER CLAUS
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).
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公开(公告)号：ES2253661T3
公开(公告)日：2006-06-01
申请号：ES03706482
申请日：2003-02-12
Applicant: BASF AG
Inventor： OLBERT GERHARD , MATTKE TORSTEN , VANDERWAEREN LUC , NEVEJANS FILIP , HAMMENECKER JAN
Abstract: Procedimiento para la obtención de fosgeno mediante reacción en fase gaseosa de monóxido de carbono y de cloro en presencia de un catalizador en lecho fijo, en uno o varios reactores (1) de forma cilíndrica, con un haz de tubos de contacto (2) dispuestos paralelamente entre sí, ordenados en la dirección longitudinal del reactor, que están fijados en sus extremos en platos de tubos (3), respectivamente con una caperuza (4) en ambos extremos del reactor (1), así como con chapas de desviación (6) dispuestas perpendicularmente con respecto a la dirección longitudinal del reactor, en cavidades intermedias (5) entre los tubos de contacto (2), que dejan libres, sobre la pared interna del reactor, orificios de paso (7) contrapuestos entre sí de manera alternativa, estando cargados los tubos de contacto (2) con el catalizador en lecho fijo, conduciéndose la mezcla de la reacción en estado gaseoso desde un extremo del reactor por una caperuza (4) a través de los tubos de contacto (2) y descargándosepor el extremo opuesto del reactor a través de una segunda caperuza (4) y conduciéndose a través de la cavidad intermedia (5) alrededor de los tubos de contacto (2) un agente intercambiador de calor líquido, caracterizado porque se dejan libres de tubos el o los reactores (1) en la zona de los orificios de paso (7) para la realización del procedimiento.
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公开(公告)号：BRPI0409086A
公开(公告)日：2006-04-11
申请号：BRPI0409086
申请日：2004-04-02
Applicant: BASF AG
Inventor： SACHWEH BERND , HUBER GUENTHER , DUDA MARK , MATTKE TORSTEN , OLBERT GERHARD
IPC: B01J37/02
Abstract: A process for coating internals in a reactor, except for the coating of electrically heatable, at least partly open-cell foams, with a catalytically active material or a precursor thereof, in which an aerosol which contains the catalytically active material or the precursor thereof as a disperse phase is provided and the aerosol is passed through the reactor at a rate in the range from 0.1 to 4 m/s, which is established so that the disperse phase of the aerosol is deposited on the internals in the reactor.
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Patent Agency Ranking
公开(公告)号：DE102004017150A1
公开(公告)日：2005-10-27
申请号：DE102004017150
申请日：2004-04-07
Applicant: BASF AG
Inventor： OLBERT GERHARD , HECHLER CLAUS
IPC: B01J8/02 , B01J19/24 , C07C45/32 , C07C45/33 , C07C45/35 , C07C45/38 , C07C47/22 , C07C51/16 , C07C51/215 , C07C51/25 , C07C57/05 , F28D9/00 , F28F3/04
Abstract: Partial oxidation in the gas phase of 3C and/or 4C precursor compounds to (meth)acrolein and/or (meth)acrylic acid in the presence of a heterogeneous particulate catalyst in a reactor having cuboidal thermoplate modules (1), a predominately cylindrical shell (4), and having sealing element(s) which are arranged such that the fluid reaction mixture only flows through the gap. Partial oxidation in the gas phase of 3C and/or 4C precursor compounds to (meth)acrolein and/or (meth)acrylic acid in the presence of a heterogeneous particulate catalyst in a reactor having cuboidal thermoplate modules which are each formed from two or more rectangular thermoplates arranged parallel to each other while in each case leaving a gap which can be filled with the heterogeneous particulate catalyst and is flowed through by the fluid reaction mixture, the heat of reaction being absorbed by a heat carrier which flows through the thermoplates and thus at least partly evaporating; having a predominately cylindrical shell which releases the pressure at the thermoplate modules, completely surrounds them and comprises a cylinder jacket and hoods (15, 16) which seal it at both ends and whose longitudinal axis is aligned parallel to the plane of the thermoplates; and having sealing element(s) which are arranged in such a way that the fluid reaction mixture, apart from flowing through the reactor interior spaces bounded by the hoods, only flows through the gap.
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公开(公告)号：PT1401566E
公开(公告)日：2005-02-28
申请号：PT02740689
申请日：2002-06-05
Applicant: BASF AG
Inventor： OLBERT GERHARD , TORSTEN MATTKE , MATTHIAS KUMMER , THOMAS RUEHL , FRANK ROSOWSKI
Abstract: A reactor for testing catalyst systems which has a plurality of catalyst tubes ( 2 ) which are arranged parallel to one another in the interior space of the reactor and whose ends are welded into tube plates and also has caps ( 3 ) at each end of the reactor which each bound a cap space ( 4 ), with a fluid reaction medium ( 5 ) being fed via one cap space ( 4 ) into the catalyst tubes ( 2 ), flowing through the catalyst tubes ( 2 ) and being discharged via the other cap space ( 4 ), and is also provided with a heat exchange medium circuit in which the heat exchange medium ( 6 ) is fed in at one end of the reactor, flows through the intermediate space between the catalyst tubes ( 2 ) and flows out at the other end of the reactor, wherein the catalyst tubes ( 2 ) are arranged in two or more catalyst tube regions ( 7 ) which are thermally separate from one another, is proposed.
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公开(公告)号：DE102004036696A1
公开(公告)日：2005-02-24
申请号：DE102004036696
申请日：2004-07-29
Applicant: BASF AG
Inventor： OLBERT GERHARD , MATTKE TORSTEN
Abstract: A gas distributor for an apparatus comprising a tank (2) with a gas inlet (3) of smaller diameter comprises a perforated, sheet metal frustoconical fitment or a fitment (8) comprising an upper cylinder (1) connected to a frustoconical section. An independent claim is included for mounting a fitment comprising welding latches to the inner wall of the tank, on to which it is screwed.
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公开(公告)号：CA2532646A1
公开(公告)日：2005-02-03
申请号：CA2532646
申请日：2004-07-21
Applicant: BASF AG
Inventor： HECHLER CLAUS , OLBERT GERHARD
Abstract: The invention relates to a reactor for partial oxidation of a fluid reaction mixture in the presence of a heterogeneous particulate catalyst. Said reacto r comprises one or several cuboid heat-transfer sheet modules (1) which are ea ch 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 t he 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 t he reactor interior spaces, defined by the caps (15, 16).
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公开(公告)号：DE50006848D1
公开(公告)日：2004-07-22
申请号：DE50006848
申请日：2000-11-03
Applicant: BASF AG
Inventor： HECHLER CLAUS , MACHHAMMER OTTO , OLBERT GERHARD , STABEL UWE , ZEHNER PETER
IPC: B01J8/02 , B01J19/24 , C07B61/00 , C07C27/00 , C07C45/33 , C07C45/35 , C07C45/37 , C07C47/22 , C07C51/235 , C07C57/05 , C07C57/055 , F28D9/00
Abstract: A process for the continuous gas-phase oxidation of C 3 - and C 4 -precursors to (meth)acrolein and/or (meth)acrylic acid in the presence of a catalyst in a reactor which has a feed for the reaction mixture at one reactor end and removal of the reaction mixture at the opposite reactor end and which is equipped with means, arranged in the interior of the reactor, for removing the heat of reaction, through which means a heat exchange composition flows and which means are in the form of heat exchanger plates, is proposed.
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