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公开(公告)号:WO2007113085A3
公开(公告)日:2008-03-13
申请号:PCT/EP2007052354
申请日:2007-03-13
Applicant: BASF AG , SCHUBERT MARKUS , MUELLER ULRICH , KIENER CHRISTOPH , TEICH FRIEDHELM , CRONE SVEN , SIMON FALK , PASTRE JOERG
Inventor: SCHUBERT MARKUS , MUELLER ULRICH , KIENER CHRISTOPH , TEICH FRIEDHELM , CRONE SVEN , SIMON FALK , PASTRE JOERG
Abstract: The invention relates to a method for producing propene from propane. Said method comprises the following steps: A) a feed gas stream (a) containing propane is prepared; B) the feed gas stream (a) containing propane, is introduced with optionally water vapour and optionally, an oxygen-containing gas stream into a dehydrogenation zone and then the propane is dehydrogenated to form propene, and a product gas stream (b) containing propane, propene, methane, ethane, ethene, hydrogen, optionally carbon monoxide, carbon dioxide, water vapour and oxygen, is obtained; C) the product gas stream (b) is cooled, optionally compressed and then water vapour is separated by condensation and a product gas stream (c) depleted in water vapour is obtained; D) the product gas stream (c) is brought into contact with a selectively active adsorber which selectively adsorbs propene in the selected adsorption conditions, and an adsorber charged with propene and a gas stream (d2) depleted in propene and containing propane, methane, ethane, ethene and hydrogen, carbon monoxide and carbon dioxide are obtained; E) a gas stream (e1) containing propene is released from the adsorber charged with propene by reducing the pressure and/or heat of the adsorber.
Abstract translation: 本发明涉及用于由丙烷制备丙烯的方法,包括步骤:A)(a)中,提供了一种含丙烷的原料气流; B)包含(a),任选的蒸汽和任选的含氧气体流中的丙烷进料气流被送入脱氢区和丙烷经受脱氢成丙烯,得到产物气流b包括丙烷,丙烯,甲烷,乙烷,乙烯,氢气,任选的一氧化碳 ,二氧化碳,获得水蒸汽和氧气; C)的产物气流(B)被冷却,冷凝,任选地,这将允许水蒸气通过冷凝分离,得到一个蒸汽贫化产物气流(获得的C); D)的产物气流(c)的具有选择性作用的吸附剂选择性吸附所选择的吸附条件下丙烯,与一个装有丙烯吸附剂和贫丙烯气流(D2)的包含丙烷,甲烷,乙烷,乙烯接触接触 和氢,得到一氧化碳和二氧化碳; E)从载有丙烯吸附剂通过减压和/或吸附剂的加热,气体流包含丙烯(E1)释放。
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公开(公告)号:AU2003240591B2
公开(公告)日:2009-06-18
申请号:AU2003240591
申请日:2003-05-02
Applicant: BASF AG
Inventor: HOFSTADT OTTO , SIMON FALK , SCHINDLER GOTZ-PETER , HESSE MICHAEL , HARTH KLAUS
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06
Abstract: The invention relates to a process for preparing a catalyst support, in which zirconium dioxide powder is mixed with a binder, if desired a pore former, if desired an acid, water and, if desired, further additives to give a kneadable composition and the composition is homogenized, shaped to produce shaped bodies, dried and calcined, wherein the binder is a monomeric, oligomeric or polymeric organosilicon compound. Suitable binders are monomeric, oligomeric or polymeric silanes, alkoxysilanes, aryloxysilanes, acryloxysilanes, oximinosilanes, halosilanes, aminoxysilanes, aminosilanes, amidosilanes, silazanes or silicones. The invention also provides the catalyst support which has been prepared in this way, a catalyst comprising the support and its use as dehydrogenation catalyst.
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公开(公告)号:BRPI0518311A2
公开(公告)日:2008-11-11
申请号:BRPI0518311
申请日:2005-11-16
Applicant: BASF AG
Inventor: CRONE SVEN , SCHINDLER GOETZ-PETER , FRITZ PETER MATTHIAS , BOELT HEINZ , SIMON FALK
Abstract: The invention provides a process for hydrogenating streams in plants for producing alkenes by catalytic dehydrogenation of light alkanes, and also an apparatus for carrying out the process. The entire hydrocarbon stream to the dehydrogenation reactor, consisting of fresh and recycled alkane, is subjected upstream of the dehydrogenation reactor to a full hydrogenation of all unsaturated hydrocarbons present therein. This drastically reduces coke formation in the dehydrogenation reactor. The energy demand for the preheating of the reactant stream to reaction temperature is reduced since the energy released in the exothermic hydrogenation remains virtually fully in the hydrocarbon stream.
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公开(公告)号:BR0309653A
公开(公告)日:2005-03-01
申请号:BR0309653
申请日:2003-05-02
Applicant: BASF AG
Inventor: HOFSTADT OTTO , HESSE MICHAEL , SCHINDLER GOETZ-PETER , HARTH KLAUS , SIMON FALK
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06 , B01J23/24 , B01J23/40 , B01J23/70 , C07C5/327
Abstract: The invention relates to a process for preparing a catalyst support, in which zirconium dioxide powder is mixed with a binder, if desired a pore former, if desired an acid, water and, if desired, further additives to give a kneadable composition and the composition is homogenized, shaped to produce shaped bodies, dried and calcined, wherein the binder is a monomeric, oligomeric or polymeric organosilicon compound. Suitable binders are monomeric, oligomeric or polymeric silanes, alkoxysilanes, aryloxysilanes, acryloxysilanes, oximinosilanes, halosilanes, aminoxysilanes, aminosilanes, amidosilanes, silazanes or silicones. The invention also provides the catalyst support which has been prepared in this way, a catalyst comprising the support and its use as dehydrogenation catalyst.
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公开(公告)号:NO20072284L
公开(公告)日:2007-08-16
申请号:NO20072284
申请日:2007-05-03
Applicant: BASF AG
Inventor: SCHINDLER GOTZ-PETER , SIMON FALK , CRONE SVEN , FRITZ PETER MATTHIAS , BOLT HEINZ
Abstract: The invention provides a process for hydrogenating streams in plants for producing alkenes by catalytic dehydrogenation of light alkanes, and also an apparatus for carrying out the process. The entire hydrocarbon stream to the dehydrogenation reactor, consisting of fresh and recycled alkane, is subjected upstream of the dehydrogenation reactor to a full hydrogenation of all unsaturated hydrocarbons present therein. This drastically reduces coke formation in the dehydrogenation reactor. The energy demand for the preheating of the reactant stream to reaction temperature is reduced since the energy released in the exothermic hydrogenation remains virtually fully in the hydrocarbon stream.
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公开(公告)号:EA008478B1
公开(公告)日:2007-06-29
申请号:EA200401445
申请日:2003-05-02
Applicant: BASF AG
Inventor: HOFSTADT OTTO , HESSE MICHAEL , SCHINDLER GOTZ-PETER , HARTH KLAUS , SIMON FALK
IPC: B01J21/06 , B01J23/62 , B01J23/24 , B01J23/40 , B01J23/63 , B01J23/70 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/327 , C07C5/333 , C07C11/06
Abstract: Изобретениеотноситсяк способуполученияносителякатализатора, вкоторомпорошокдиоксидациркониясмешиваютсосвязующим, принеобходимости, спорообразователем, принеобходимости, скислотой, водойи, принеобходимости, другимидобавкамис получениемспособнойк замешиваниюкомпозициии композициюгомогенизируют, формуютдляполученияформованныхэлементов, сушати прокаливают, причемсвязующимявляетсямономерное, олигомерноеилиполимерноекремнийорганическоесоединение. Пригоднымисвязующимиявляютсямономерные, олигомерныеилиполимерныесиланы, алкоксисиланы, арилоксисиланы, акрилоксисиланы, оксиминосиланы, галогенсиланы, аминоксисиланы, аминосиланы, амидосиланы, силазаныи силиконы. Изобретениетакжекасаетсяносителякатализатора, которыйполучаютупомянутымспособом, катализатора, содержащегоноситель, иегопримененияв качествекатализаторадегидрирования.
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公开(公告)号:CA2558547A1
公开(公告)日:2005-10-20
申请号:CA2558547
申请日:2005-03-22
Applicant: BASF AG
Inventor: VORBERG GERALD , SCHINDLER GOETZ-PETER , HESSE MICHAEL , SIMON FALK , WALSDORFF CHRISTIAN
Abstract: The invention relates to a catalyst for the oxidation of hydrogen in a hydrocarbon dehydrogenation process. Said catalyst is carried on a-aluminum oxide and contains 0.01 to 0.1 percent by weight of platinum and 0.01 to 0.1 percent by weight of pewter relative to the total weight of the catalyst. Al so disclosed are a method for oxygenating hydrogen and a method for dehydrogenating hydrocarbons with an integrated oxidation process using said catalyst.
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公开(公告)号:CA2482790A1
公开(公告)日:2003-11-13
申请号:CA2482790
申请日:2003-05-02
Applicant: BASF AG
Inventor: HESSE MICHAEL , SCHINDLER GOETZ-PETER , HARTH KLAUS , SIMON FALK , HOFSTADT OTTO
IPC: B01J23/62 , B01J21/06 , B01J23/63 , B01J35/00 , B01J35/10 , B01J37/00 , C07B61/00 , C07C5/333 , C07C11/06 , B01J23/24 , C07C5/327 , B01J23/40 , B01J23/70
Abstract: The invention relates to a method for the production of a catalyst carrier, wherein Zirconium dioxide powder is mixed with a binding agent, optionally a pore forming agent, optionally an acid, water and optionally other additives to form a kneadable mass, said mass is homogenized in order to form shaped bodies, dried and calcinated. The binding agent is a monomer, oligomer or polymer organosilicon compound.Suitable binding agents are monomer, oligomer or polymer silanes, alkoxysilanes, aryloxysilanes, acryloxysilanes, oximinosilanes, halogensilanes, aminoxysilanes, aminosilanes, amidosilanes, silazanes or silicones. The invention also relates to a catalyst carrier thu s produced, a catalyst containing said carrier and the use thereof as a dehydrogenation catalyst.
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公开(公告)号:AU2002365634A1
公开(公告)日:2003-06-17
申请号:AU2002365634
申请日:2002-12-04
Applicant: BASF AG
Inventor: SIMON FALK , HARTH KLAUS , SCHINDLER GOTZ-PETER , WALSDORFF CHRISTIAN , KUHRS CHRISTIAN
IPC: C07C17/02 , C07C17/15 , C07C17/152 , C07C17/156 , C07C17/158 , C07C17/25 , C07C17/38 , C07C19/045 , C07C21/06
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公开(公告)号:DE10159615A1
公开(公告)日:2003-06-12
申请号:DE10159615
申请日:2001-12-05
Applicant: BASF AG
Inventor: HARTH KLAUS , SCHINDLER GOETZ-PETER , WALSDORFF CHRISTIAN , KUHRS CHRISTIAN , SIMON FALK
IPC: C07C17/02 , C07C17/15 , C07C17/152 , C07C17/156 , C07C17/158 , C07C17/25 , C07C17/38 , C07C19/045 , C07C21/06
Abstract: The invention relates to a method for the production of 1,2-dichloroethane, comprising the following steps: (A) feeding a feed gas flow containing an ethane into a dehydrogenation zone; dehydrogenating the ethane into ethene while obtaining a product gas flow containing ethane, ethene and minor constituents; (B) feeding the dehydrogenated product gas flow containing the ethane and ethene into a flow or several partial flows, optionally after separating the minor constituents, in one or more chlorination zones; chlorinating ethene into 1,2-dichloroethane while obtaining one or more product gas flows containing 1,2-dichloroethane, ethane and optionally other minor; obtaining 1,2-dichloroethane and one or more circuit gas flows containing ethane and recirculating the circuit gas flow(s) containing ethane to the ethane dehydrogenation.
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