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    METHOD FOR TREATING CATALYTIC CONVERTER PREFORMS AND CATALYTIC CONVERTER PREFORMS WITH ENHANCED MECHANICAL STRENGTH
    52.
    发明专利
    METHOD FOR TREATING CATALYTIC CONVERTER PREFORMS AND CATALYTIC CONVERTER PREFORMS WITH ENHANCED MECHANICAL STRENGTH 未知

    公开(公告)号：IN1366DEN2015A

    公开(公告)日：2015-07-03

    申请号：IN1366DEN2015

    申请日：2015-02-19

    Applicant: BASF SE

    Inventor： HEIDEMANN THOMAS ,  ÖZKOZANOGLU CLAUDIA

    IPC: B01J21/02 ,  B01J21/04 ,  B01J29/70

    Abstract: The present invention specifies a method for treating catalytic converter preforms particularly to increase the mechanical strength thereof said method comprising the following steps: a) provision of prepared catalytic converter preforms; b) immersion of the catalytic converter preforms together with a peptising agent in a volume of liquid not exceeding the theoretical water absorption of the catalytic converter preform; c) thermal treatment of the immersed catalytic converter preforms at 50°C to 250°C; and d) calcination of the thermally treated catalytic converter preforms at 250°C to 600°C. Furthermore a catalytic converter preform with enhanced mechanical strength is created which can be produced using the method according to the invention. The present invention further relates to the use of catalytic converter preforms according to the invention for the production of amines and in solid bed reactors or fluidized bed reactors and to a chemical synthesis method in the presence of catalytic converter preforms according to the present invention.

    Procedimiento para la aminación directa de hidrocarburos para dar aminohidrocarburos con separación electroquímica de hidrógeno y conversión electroquímica del hidrógeno en agua
    55.
    发明专利
    Procedimiento para la aminación directa de hidrocarburos para dar aminohidrocarburos con separación electroquímica de hidrógeno y conversión electroquímica del hidrógeno en agua 未知

    公开(公告)号：ES2533702T3

    公开(公告)日：2015-04-14

    申请号：ES10731732

    申请日：2010-07-07

    Applicant: BASF SE

    Inventor： KUBANEK PETR ,  PANCHENKO ALEXANDER ,  FISCHER ANDREAS ,  HEIDEMANN THOMAS

    IPC: C25B3/23 ,  C07C209/02

    Abstract: Procedimiento para la aminación directa de hidrocarburos para dar aminohidrocarburos mediante reacción de un flujo de productos de partida E, que contiene al menos un hidrocarburo y al menos un reactivo de aminación, para dar una mezcla de reacción R, que contiene aminohidrocarburo e hidrógeno en una zona de reacción RZ, y separación electroquímica al menos de una parte del hidrógeno producido durante la reacción a partir la mezcla de reacción R por medio de un conjunto de membrana-electrodos hermético a los gases, que presenta al menos una membrana conductora de protones de manera selectiva y en cada lado de la membrana al menos un catalizador de electrodo, en el que en el lado del material retenido de la membrana al menos una parte del hidrógeno se oxida en el catalizador de ánodo para dar protones y los protones tras atravesar la membrana en el lado del material permeado se hacen reaccionar en el catalizador de cátodo con oxígeno para dar agua, procediendo el oxígeno de un flujo O que contiene oxígeno, que se pone en contacto con el lado del material permeado de la membrana.

    Method for producing aromatic compounds from methane
    57.
    发明专利
    Method for producing aromatic compounds from methane 未知

    公开(公告)号：AU2011290935B2

    公开(公告)日：2014-02-27

    申请号：AU2011290935

    申请日：2011-07-20

    Applicant: BASF SE

    Inventor： SCHNEIDER CHRISTIAN ,  AHRENS SEBASTIAN ,  BACHMANN KATI ,  COELHO TSOU JOANA ,  HEIDEMANN THOMAS ,  WENTINK ANNEBART ENGBERT

    IPC: C07C2/76

    Abstract: The invention relates to a method for carrying out endothermic, heterogeneously catalyzed reactions during which the reactants are reacted in the presence of a mixture of inert heat exchanger particles and catalyst particles, the catalyst particles being regenerated at regular intervals in a non-oxidative atmosphere and the required reaction heat being supplied by separating the inert heat exchanger particles, heating the heat exchanger particles in a heating zone and returning the heated heat exchanger particles to the reaction zone. The method according to the invention is particularly suitable for the non-oxidative dehydroaromatization of C

    58.
    发明专利
    未知

    公开(公告)号：AT520647T

    公开(公告)日：2011-09-15

    申请号：AT08841980

    申请日：2008-10-14

    Applicant: BASF SE

    Inventor： SIGL MARCUS ,  HEIDEMANN THOMAS

    IPC: C07C209/16 ,  C07C211/07

    Abstract: A process for preparing a primary amine with a tertiary alpha-carbon atom by reacting a tertiary alcohol with ammonia in the presence of a heterogeneous catalyst, by performing the reaction in the presence of a non-microporous, non-zeolitic aluminosilicate as a catalyst, where the aluminosilicate has a molar Al/Si ratio in the range from 0.1 to 30.

    59.
    发明专利
    未知

    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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