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公开(公告)号:ES2381863T3
公开(公告)日:2012-06-01
申请号:ES06830823
申请日:2006-12-22
Applicant: BASF SE
Inventor: BECKER MICHAEL , SALDEN AXEL , STAECK BIANCA , HENKELMANN JOCHEN , SPRINGMANN STEFFEN , VAN LAAR FREDERIK , RUPPEL WILHELM , RESCH PETER , BENDER MICHAEL
Abstract: Método para la conversión de un hidrocarburo aromático, o de una mezcla de hidrocarburos aromáticos, que contiene compuestos aromáticos sulfurados, en cuyo caso en un primer paso opcionalmente en presencia de hidrógeno, se disminuye el contenido de compuestos aromáticos sulfurados empleando un agente desulfurante que contiene cobre y cinc en una proporción atómica de 1 : 0,3 a 1 : 10 (paso a), y en un segundo paso el hidrocarburo aromático, o la mezcla de los hidrocarburos aromáticos, se hidrogena en presencia de un catalizador de rutenio soportado y en presencia de hidrógeno (paso b).
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公开(公告)号:DE502004010566D1
公开(公告)日:2010-02-11
申请号:DE502004010566
申请日:2004-01-31
Applicant: BASF SE
Inventor: HEIDEMANN THOMAS , ULONSKA ARMIN , STAECK BIANCA
IPC: C07C2/10
Abstract: In a nickel-catalysed method for the oligomerization of 4-8C alkenes in a series of 2 or more reactors operating under adiabatic conditions, the feed stream is split and the part-streams are fed into at least 2 of the reactors with the addition of fresh feed so that the temperature in any reactor is not more than 20[deg]C above that in any of the other reactors. A method for the production of oligomers of 4-8C alkenes from a hydrocarbon feed stream containing such alkenes, on a nickel-containing heterogeneous catalyst in a series of 2 or more reactors operating under adiabatic conditions at 30-280[deg]C and 1-300 bar, where: (a) the feed stream is introduced into reaction zone 1 at a temperature T1, (b) the temperature increases in each zone, and (c) if this increase is more than T1 + 20[deg]C, the temperature is adjusted to within the range T1 +- 20[deg]C before the mixture is fed into the next zone. In this method, the feed stream is split and the part-streams are fed into at least two of the reactors with the addition of fresh feed so that the temperature in any one reactor is not more than 20[deg]C above that in any of the other reactors.
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公开(公告)号:ES2360945T3
公开(公告)日:2011-06-10
申请号:ES06100368
申请日:2006-01-16
Applicant: BASF SE
Inventor: STAECK BIANCA , KAIBEL GERD , POPLOW FRANK , ZEHNER PETER
Abstract: Reactor para realizar reacciones de fase gaseosas, reacciones gas/líquido, líquido/líquido, líquido/sólido o gas/líquido/sólido con un interior del reactor que se encuentra dividido en dos o en más cámaras de reacción que se encuentran completamente separadas unas de otras, caracterizado porque la separación del interior del reactor tiene lugar mediante una o varias paredes divisorias que se encuentran dispuestas en la dirección longitudinal del reactor, donde dichas paredes divisorias se encuentran diseñadas como una chapa plana o predominantemente plana que se encuentra insertada en el interior del reactor.
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公开(公告)号:DE502006009079D1
公开(公告)日:2011-04-28
申请号:DE502006009079
申请日:2006-01-16
Applicant: BASF SE
Inventor: STAECK BIANCA , KAIBEL GERD , POPLOW FRANK , ZEHNER PETER
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公开(公告)号:SG168520A1
公开(公告)日:2011-02-28
申请号:SG2010095487
申请日:2006-12-22
Applicant: BASF SE
Inventor: BECKER MICHAEL , SALDEN AXEL , STAECK BIANCA , HENKELMANN JOCHEN , SPRINGMANN STEFFEN , VAN LAAR FREDERIK , RUPPEL WILHELM , RESCH PETER , BENDER MICHAEL
Abstract: The present invention relates to a process for converting an aromatic hydrocarbon which comprises aromatic sulfur compounds, or a mixture of aromatic hydrocarbons which comprises aromatic sulfur compounds, if appropriate in the presence of hydrogen, wherein, in a first step, aromatic sulfur compounds are removed (step a), and, in a second step, the aromatic hydrocarbon or the mixture of aromatic hydrocarbons is hydrogenated in the presence of a supported ruthenium catalyst in the presence of hydrogen (step b). (No suitable figure)
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公开(公告)号:AT453607T
公开(公告)日:2010-01-15
申请号:AT04002145
申请日:2004-01-31
Applicant: BASF SE
Inventor: HEIDEMANN THOMAS , ULONSKA ARMIN , STAECK BIANCA
IPC: C07C2/10
Abstract: In a nickel-catalysed method for the oligomerization of 4-8C alkenes in a series of 2 or more reactors operating under adiabatic conditions, the feed stream is split and the part-streams are fed into at least 2 of the reactors with the addition of fresh feed so that the temperature in any reactor is not more than 20[deg]C above that in any of the other reactors. A method for the production of oligomers of 4-8C alkenes from a hydrocarbon feed stream containing such alkenes, on a nickel-containing heterogeneous catalyst in a series of 2 or more reactors operating under adiabatic conditions at 30-280[deg]C and 1-300 bar, where: (a) the feed stream is introduced into reaction zone 1 at a temperature T1, (b) the temperature increases in each zone, and (c) if this increase is more than T1 + 20[deg]C, the temperature is adjusted to within the range T1 +- 20[deg]C before the mixture is fed into the next zone. In this method, the feed stream is split and the part-streams are fed into at least two of the reactors with the addition of fresh feed so that the temperature in any one reactor is not more than 20[deg]C above that in any of the other reactors.
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公开(公告)号:PL1966111T3
公开(公告)日:2012-07-31
申请号:PL06830823
申请日:2006-12-22
Applicant: BASF SE
Inventor: BECKER MICHAEL , SALDEN AXEL , STAECK BIANCA , HENKELMANN JOCHEN , SPRINGMANN STEFFEN , VAN LAAR FREDERIK , RUPPEL WILHELM , RESCH PETER , BENDER MICHAEL
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公开(公告)号:AT543791T
公开(公告)日:2012-02-15
申请号:AT06830823
申请日:2006-12-22
Applicant: BASF SE
Inventor: BECKER MICHAEL , SALDEN AXEL , STAECK BIANCA , HENKELMANN JOCHEN , SPRINGMANN STEFFEN , VAN LAAR FREDERIK , RUPPEL WILHELM , RESCH PETER , BENDER MICHAEL
Abstract: Conversion of an aromatic hydrocarbon or its mixture containing sulfur containing aromatic compounds comprises lowering the content of the sulfur containing compound in the presence of hydrogen, and hydrogenating the aromatic hydrocarbon or its mixture in the presence of a ruthenium catalyst and hydrogen. An independent claim is included for a method for desulfurization of the aromatic hydrocarbon or its mixture comprising lowering the content of sulfur containing aromatic compound to = 70 ppb using desulfurization agent, where the total amount of the sulfur containing aromatic compound is = 200 ppb, and the desulfurization agent contains copper oxide (35-45 wt.%), zinc oxide (35-45 wt.%) and alumina (10-30 wt.%).
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公开(公告)号:AT501789T
公开(公告)日:2011-04-15
申请号:AT06100368
申请日:2006-01-16
Applicant: BASF SE
Inventor: STAECK BIANCA , KAIBEL GERD , POPLOW FRANK , ZEHNER PETER
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公开(公告)号:UA94081C2
公开(公告)日:2011-04-11
申请号:UAA200809666
申请日:2006-12-22
Applicant: BASF SE
Inventor: BECKER MICHAEL , SALDEN AXEL , STAECK BIANCA , HENKELMANN JOCHEN , SPRINGMANN STEFFEN , VAN LAAR FREDERIK , RUPPEL WILHELM , RESCH PETER , BENDER MICHAEL
Abstract: Данноеизобретениекасаетсяспособапреобразованияароматическогоуглеводорода, содержащегоароматическиесоединениясерыилисмесиароматическихуглеводородов, содержащейароматическиесоединениясеры, причемнапервойстадииизвлекаютароматическиесоединениясеры (стадияа), анавторойстадииароматическийуглеводородилисмесьароматическихуглеводородовгидрируютв присутствиинанесенногонаносительрутениевогокатализаторав присутствииводорода (стадия b).
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