СПОСОБ ПОЛУЧЕНИЯ БУТАДИЕНА ИЗ н-БУТАНА

    公开(公告)号:EA012614B1

    公开(公告)日:2009-10-30

    申请号:EA200701506

    申请日:2006-01-16

    Applicant: BASF AG

    Abstract: Способполучениябутадиенаизн-бутана, включающийследующиестадии: А) подготовкаисходногогазовогопотокаа, содержащегон-бутан; В) подачасодержащегон-бутанисходногогазовогопотокаа, поменьшеймере, впервуюзонудегидрированияи неокислительноекаталитическоедегидрированиен-бутана, причемполучаютгазовыйпотокпродукта b, содержащийн-бутан, 1-бутен, 2-бутен, бутадиен, водород, низкокипящиепримеси, приизвестныхусловияхоксидыуглеродаи приизвестныхусловияхводянойпар; С) подводгазовогопотокапродукта b неокислительногокаталитическогодегидрированияи кислородсодержащегогаза, поменьшеймере, вовторуюзонудегидрированияи окислительноедегидрированиен-бутана, 1-бутенаи 2-бутена, причемполучаютгазовыйпотокпродуктас, содержащийн-бутан, 2-бутен, бутадиен, низкокипящиепримеси, оксидыуглеродаи водянойпар, сболеевысокимсодержаниембутадиена, чемв газовомпотокепродукта b; D) отделениенизкокипящихпримесейи водяногопара, причемполучаетсягазовыйпотокС-продукта d, восновномсостоящийизн-бутана, 2-бутенаи бутадиена; E) разделениеэкстрактивнойректификациейгазовогопотокаС-продукта d напоток el, состоящийв основномизн-бутанаи 2-бутена, ипотокценногопродуктае2, восновномсостоящийизбутадиена; F) возвратпотока el впервуюзонудегидрирования.

    СПОСОБ КАТАЛИТИЧЕСКОГО ДЕГИДРИРОВАНИЯ ЛЕГКИХ АЛКАНОВ

    公开(公告)号:EA012015B1

    公开(公告)日:2009-06-30

    申请号:EA200700910

    申请日:2005-11-16

    Applicant: BASF AG

    Abstract: Объектомизобретенияявляетсяспособкаталитическогодегидрированиялегкихалканов, вкоторомвесьсостоящийизсвежегои повторноиспользованногоалканапотокуглеводородовк реакторудлядегидрированияещедореакторадлядегидрированияподвергаетсяполномугидрированиювсехсодержащихсяв немненасыщенныхуглеводородов. Благодаряэтомув реакторедлядегидрированияощутимоуменьшаетсякоксообразование. Сокращаютсяэнергетическиезатратынаподогревпотокаэдуктадотемпературыреакции, таккакосвобожденнаяприэкзотермическомгидрированииэнергияпочтиполностьюостаетсяв потокеуглеводородов.

    13.
    发明专利
    未知

    公开(公告)号:NO327435B1

    公开(公告)日:2009-06-29

    申请号:NO20044561

    申请日:2004-10-22

    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.

    14.
    发明专利
    未知

    公开(公告)号:DE102006017908A1

    公开(公告)日:2007-10-25

    申请号:DE102006017908

    申请日:2006-04-18

    Applicant: BASF AG LINDE AG

    Abstract: The invention relates to a method and a device for the controlled regeneration of a catalyst and of a fired reactor, especially a catalyst and a reactor in a plant for producing olefins from a hydrocarbon-containing charge. During the regeneration phase of the catalyst for recovering the catalytic activity, the burners of the reactor are switched off. After the regeneration phase, the burners are re-ignited by means of inbuilt pilot burners. The pilot burners are monitored and their capacity is adjusted in such a manner that the heat loss of the reactor during the regeneration phase of the catalyst is compensated for.

    PROCEDIMIENTO Y DISPOSITIVO PARA LA HIDROGENACION COMPLETA DE UNA CORRIENTE DE HIDROCARBURO.

    公开(公告)号:MX2007005043A

    公开(公告)日:2007-06-19

    申请号:MX2007005043

    申请日:2005-11-16

    Applicant: BASF AG

    Abstract: El objeto de la invencion es un procedimiento para la hidrogenacion completa de corrientes de sustancias en plantas para la produccion de alquenos por deshidrogenacion catalitica de alcanos livianos, asi como un dispositivo para la realizacion del procedimiento. Toda la corriente de hidrocarburo hacia el reactor de deshidrogenacion, que se compone de alcano fresco y alcano reciclado, es sometida todavia antes de entrar en el reactor de deshidrogenacion a una hidrogenacion completa de todos los hidrocarburos no saturados contenidos en ella. De este modo se alcanza reducir drasticamente la formacion de coque en el reactor de deshidrogenacion. La energia necesaria para el precalentamiento de la corriente de eductos a la temperatura de reaccion es reducida, puesto que la energia librada en la hidrogenacion exotermica permanece caso por completo en la corriente de hidrocarburo.

    17.
    发明专利
    未知

    公开(公告)号:BRPI0606630A2

    公开(公告)日:2010-01-19

    申请号:BRPI0606630

    申请日:2006-01-16

    Applicant: BASF AG

    Abstract: A process for preparing butadiene, comprising A) providing a stream (a) comprising n-butane; B) feeding stream (a) comprising into at least one first dehydrogenation zone and nonoxidatively catalytically dehydrogenating n-butane to obtain a stream (b) comprising n-butane, 1-butene, 2-butene, butadiene, hydrogen and low-boiling secondary constituents; C) feeding stream (b) and an oxygenous gas into at least one second dehydrogenation zone and oxidatively dehydrogenating n-butane, 1-butene and 2-butene to obtain a stream (c) comprising n-butane, 2-butene, butadiene, low-boiling secondary constituents, carbon oxides and steam, wherein stream (c) has a higher content of butadiene than stream (b); D) removing the low-boiling secondary constituents and steam to obtain a stream (d) substantially consisting of n-butane, 2-butene and butadiene; E) separating stream (d) into a stream (e1) consisting substantially of n-butane and 2-butene and a stream (e2) consisting substantially of butadiene by extractive distillation; F) recycling stream (e1) into the first dehydrogenation zone.

    18.
    发明专利
    未知

    公开(公告)号:DE102006017906A1

    公开(公告)日:2007-10-25

    申请号:DE102006017906

    申请日:2006-04-18

    Applicant: LINDE AG BASF AG

    Abstract: The invention relates to a method and a device for putting into service a reactor and a catalyst, especially a catalyst and a reactor for dehydrogenating a hydrocarbon-containing charge in a plant for producing olefins. Before being put into service, the catalyst and the reactor run through a plurality of oxidation and reduction phases, thereby releasing the chloride contained in the catalyst. The released chloride is carried off into the atmosphere in a gaseous form.

    METHOD AND DEVICE FOR COMPLETELY HYDROGENATING A HYDROCARBONFLOW

    公开(公告)号:CA2586321A1

    公开(公告)日:2006-05-26

    申请号:CA2586321

    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.

Patent Agency Ranking