31.
    发明专利
    未知

    公开(公告)号:DE10315215A1

    公开(公告)日:2004-10-14

    申请号:DE10315215

    申请日:2003-04-03

    Applicant: BASF AG

    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.

    IN SITU RECOATING OF CATALYST BEDS
    32.
    发明专利

    公开(公告)号:CA2520832A1

    公开(公告)日:2004-10-14

    申请号:CA2520832

    申请日:2004-04-02

    Applicant: BASF AG

    Abstract: The invention relates to a method for coating internal fittings in a reactor , except for electrically heatable, at least partly open-cell foams, with a catalytically active material or a precursor therefor. According to said method, aerosol containing the catalytically active material or the precurso r therefor as a dispersed phase is provided and is directed through the reacto r at a speed which is set in such a way that the dispersed phase of the aeroso l deposits on the internal fittings of the reactor.

    Method for the production of a catalyst containing vanadium, phosphorus, and oxygen

    公开(公告)号:AU2003212333A8

    公开(公告)日:2003-09-29

    申请号:AU2003212333

    申请日:2003-03-12

    Applicant: BASF AG

    Abstract: Disclosed is a method for producing a catalyst containing vanadium, phosphorus, and oxygen, which is used for oxidizing the gas phase of a hydrocarbon having at least four carbon atoms to maleic anhydride. According to the inventive method, a corresponding catalyst precursor which contains vanadium, phosphorus, and oxygen and is provided with particles having an average diameter of at least 2 mm is converted into a catalytically active form by means of calcination, and a flow of the catalyst precursor is transported on a conveyor belt across at least one calcination area over a distance 1 n at an essentially steady speed in order to be calcinated. The variation over time of the gas temperature in relation to the set point value amounts to n /2 of the calcination area, while the local difference in the gas temperature between any positions in the area of the flow of the catalyst precursor, which is located within the second half 1 n /2 of the calcination area, amounts to

    СПОСОБ ПОЛУЧЕНИЯ БУТАДИЕНА И 1-БУТЕНА

    公开(公告)号:EA009785B1

    公开(公告)日:2008-04-28

    申请号:EA200601232

    申请日:2004-12-30

    Applicant: BASF AG

    Abstract: Изобретениекасаетсяспособаполучениябутадиенаизн-бутана, включающегоследующиестадии: A) подготовкаисходногогазовогопотокаа, содержащегон-бутан; B) подачасодержащегон-бутанзагрузочногогазовогопотокаа поменьшеймерев первуюзонудегидрированияи неокислительноекаталитическоедегидрированиен-бутана, причемполучаютпотокгазообразныхпродуктов b, содержащийн-бутан, 1-бутен, 2-бутен, бутадиен, водород, низкокипящиепримесии, вслучаенеобходимости, водянойпар; C) подачапотокагазообразныхпродуктов b неокислительногокаталитическогодегидрированияи содержащегокислородгазапоменьшеймеревовторуюзонудегидрированияи окислительноедегидрированиен-бутана, 1-бутенаи 2-бутена, причемполучаютпотокгазообразныхпродуктовс, содержащийн-бутан, 2-бутен, бутадиен, водород, низкокипящиепримесии водянойпар, содержаниебутадиенав которомвыше, чемв потокегазообразныхпродуктов b; D) отделениеводорода, низкокипящихпримесейи водяногопара, причемполучаютпотокС-газообразныхпродуктов d, которыйв основномсостоитизн-бутана, 2-бутенаи бутадиена; E) разделениепотокаС-газообразныхпродуктов d насостоящийв основномизн-бутанаи 2-бутанапоток e1 инасостоящийв основномизбутадиенапотокцелевогопродуктае2 посредствомэкстракционнойдистилляции; F) подачасостоящегов основномизн-бутанаи 2-бутенапотокае1 исодержащего 1-бутени 2-бутенциркуляционногопотока g взонудистилляциии разделениенабогатый 1-бутеномпотокцелевогопродукта f1, содержащий 2-бутени н-бутанрециркуляционныйпоток f2 исодержащий 2-бутенпоток f3 ирециркуляциярециркуляционногопотока f2 напервуюзонудегидрирования; G) подачасодержащего 2-бутенпотока f3 взону

    36.
    发明专利
    未知

    公开(公告)号:BRPI0418222A

    公开(公告)日:2007-04-27

    申请号:BRPI0418222

    申请日:2004-12-30

    Applicant: BASF AG

    Abstract: The disclosure involves a process for preparing butadiene from n-butane. In the process, n-butane is first dehydrogenated autothermally under nonoxidative conditions to form a gas stream. The gas stream is then oxidatively dehydrogenated to form a second gas stream. From the second gas stream, a third gas stream containing n-butane, 2-butene and butadiene is obtained. From the third gas stream, a butadiene/butaine product stream is obtained and remaining n-butane and 2-butene is recycled into the first dehydrogenation zone.

    37.
    发明专利
    未知

    公开(公告)号:DE102004059356A1

    公开(公告)日:2006-06-14

    申请号:DE102004059356

    申请日:2004-12-09

    Applicant: BASF AG

    Abstract: A process for preparing butadiene, comprising nonoxidatively dehydrogenating n-butane from a stream (a) in a first dehydrogenation zone to obtain stream (b) comprising 1-butene and 2-butene; oxidatively dehydrogenating the 1-butene and 2-butene of (b) in the presence of an oxygenous gas in a second dehydrogenation zone to obtain stream (c) comprising n-butane, butadiene, hydrogen, carbon dioxide, and steam; compressing and cooling (c) to obtain stream (d2) comprising n-butane, butadiene, hydrogen, carbon dioxide, and steam; extractively distilling (d2) into stream (e1) comprising butadiene and stream (e2) comprising n-butane, hydrogen, carbon dioxide, and steam; compressing and cooling (e2) to obtain stream (f1) comprising n-butane and water and stream (f2) comprising n-butane, hydrogen, and carbon dioxide; cooling (f2) to obtain stream (g1) comprising n-butane and stream (g2) comprising carbon dioxide and hydrogen; phase separating water from (f1) to obtain stream (h1) comprising n-butane; and recycling (h1) into the first dehydrogenation zone.

    PROCEDIMIENTO PARA PRODUCIR ANHIDRIDO DEL ACIDO MALEICO.

    公开(公告)号:ES2238589T3

    公开(公告)日:2005-09-01

    申请号:ES02754895

    申请日:2002-07-17

    Applicant: BASF AG

    Abstract: Procedimiento para la producción de anhídrido del ácido maleico mediante la oxidación en fase gaseosa, catalítica heterogénea, de una corriente de hidrocarburos que contiene n-buteno con gases que contienen oxígeno en un reactor tubular con dos zonas de reacción consecutivas, de modo que la primera zona de reacción, del lado de los eductos, contiene al menos un catalizador, que es adecuado para la oxideshidrogenación de los n-butenos para dar 1, 3-butadieno y la segunda zona de reacción, del lado de los productos, contiene al menos un catalizador que es adecuado para la oxidación de 1, 3- butadieno para dar anhídrido del ácido maleico, caracterizado porque se utiliza un reactor tubular, que presenta al menos un circuito de fluido térmico en la región de la primera zona de reacción, del lado de los eductos, y al menos otro circuito de fluido térmico en la región de la segunda zona de reacción, del lado de los productos.

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