PROCESS FOR THE EPOXIDATION OF OLEFINS

    公开(公告)号:MY131852A

    公开(公告)日:2007-09-28

    申请号:MYPI20033684

    申请日:2003-09-26

    Abstract: THE PRESENT INVENTION REFERS TO A CONTINUOS PROCESS FOR THE EPOXIDATION OF OLEFINS WITH HYDROGEN PEROXIDE IN PRESENCE OF A HETEROGENEOUS CATALYST PROMOTING THE EPOXIDATION REACTION.WHEREBY THE AQUEOUS REACTION MIXTURE COMPRISES: I) AN OLEFIN;II) HYDROGEN PEROXIDE; III) LESS THAN 100 WPPM OF ALKALI METALS. EARTH ALKALI METALS, BOTH IRRESPECTIVE WHETHER IN IONIC, COMPLEX OR COVALENTLY BONDED FORM, BASES OR CATIONS OF BASES HAVING A PKB OF LESS THAN 4.5, OR COMBINATIONS THEREOF; AND IV) AT LEAST 100 WPPM OF BASES OR CATIONS OF BASES HAVING A PKB OF AT LEAST 4.5 OR COMBINATIONS THEREOF,WHEREBY THE WPPM ARE BASED ON THE TOTAL WEIGHT OF HYDROGEN PEROXIDE IN THE REACTION MIXTURE.

    PROCESO PARA LA EPOXIDACION DE OLEFINAS

    公开(公告)号:AR032928A1

    公开(公告)日:2003-12-03

    申请号:ARP020100746

    申请日:2002-03-01

    Abstract: Un proceso para la epoxidacion catalítica de olefinas con peroxido de hidrogeno en un sistema de reaccion de flujo continuo, donde la mezcla de reaccion se hace pasar a través de un lecho fijo de catalizador en el interior de un reactor equipado con dispositivos de enfriamiento mientras se mantiene un perfil térmico dentro del reactor de modo tal que la temperatura del medio de enfriamiento del dispositivo de enfriamiento sea de al menos 40 degree C y la temperatura máxima dentro del lecho de catalizador sea de 60 degree C como máximo.

    56.
    发明专利
    未知

    公开(公告)号:BR9804474A

    公开(公告)日:2000-02-29

    申请号:BR9804474

    申请日:1998-11-06

    Applicant: DEGUSSA

    Abstract: Process for producing 5- or 6-membered cyclic ethers (anhydropolyols) comprises subjecting polyols having at least 4 C atoms and at least 2 OH groups to cyclodehydration at at least 100 degrees C in the presence of water, an acid catalyst, an acid-stable hydrogenation catalyst and hydrogen. Preferably the reaction temperature is 100-380 degrees C, preferably 180-280 degrees C. The H2 pressure is 1-20 MPa, preferably 3-10 MPa. The hydrogenation catalyst comprises Ru, Rh, Pd and/or Pt as metals or metal compounds. The hydrogenation catalyst is used in an amount of 0.001-10 (preferably 0.01-1) wt.% based on the polyol. The acid catalyst is a 1-10C aliphatic carboxylic acid, preferably formic, acetic or propionic acid. The acid catalyst is used in an amount of 0.1-20 (especially 0.5-10) wt.% based on the polyol. The polyol is a tetritol, pentitol or hexitol.

    59.
    发明专利
    未知

    公开(公告)号:DK0659733T3

    公开(公告)日:1998-01-05

    申请号:DK94118077

    申请日:1994-11-17

    Applicant: DEGUSSA

    Abstract: 3-Aminomethyl-3,5,5-trimethylcyclohexylamine (isophoronediamine) is a raw material which is used industrially for various synthetic resins. Isophoronediamine is used as a cis/trans isomer mixture, the cis/trans isomer ratio influencing the properties. The invention shows a way of controlling the isomer ratio in the preparation of isophoronediamine by aminating hydrogenation of 3-cyano-3,5,5-trimethylcyclohexanone (isophoronenitrile) in the presence of ammonia, H2 and a catalyst. The reaction is carried out in two temperature stages, namely first at 10 to 90 DEG C and then at 90 to 150 DEG C with a temperature difference between both stages of at least 30 DEG C, the contact time in the first stage being shorter than in the second. By lowering the temperature in the first stage the cis/trans ratio is increased.

    60.
    发明专利
    未知

    公开(公告)号:AT156801T

    公开(公告)日:1997-08-15

    申请号:AT94118077

    申请日:1994-11-17

    Applicant: DEGUSSA

    Abstract: 3-Aminomethyl-3,5,5-trimethylcyclohexylamine (isophoronediamine) is a raw material which is used industrially for various synthetic resins. Isophoronediamine is used as a cis/trans isomer mixture, the cis/trans isomer ratio influencing the properties. The invention shows a way of controlling the isomer ratio in the preparation of isophoronediamine by aminating hydrogenation of 3-cyano-3,5,5-trimethylcyclohexanone (isophoronenitrile) in the presence of ammonia, H2 and a catalyst. The reaction is carried out in two temperature stages, namely first at 10 to 90 DEG C and then at 90 to 150 DEG C with a temperature difference between both stages of at least 30 DEG C, the contact time in the first stage being shorter than in the second. By lowering the temperature in the first stage the cis/trans ratio is increased.

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