METHOD FOR PRODUCING PROPENE FROM PROPANE
    1.
    发明申请
    METHOD FOR PRODUCING PROPENE FROM PROPANE 审中-公开
    用于生产丙烯丙烷

    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

    CPC classification number: C07C5/333 C07C7/12 C07C7/13 C07C11/06

    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。

    3.
    发明专利
    未知

    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

    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.

    4.
    发明专利
    未知

    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

    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.

    5.
    发明专利
    未知

    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

    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.

    КАТАЛИЗАТОР ДЕГИДРИРОВАНИЯ И СПОСОБ ПОЛУЧЕНИЯ НОСИТЕЛЯ КАТАЛИЗАТОРА ДЕГИДРИРОВАНИЯ

    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

    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.

    10.
    发明专利
    未知

    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

    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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