2.
    发明专利
    未知

    公开(公告)号:FR2787791B1

    公开(公告)日:2001-05-11

    申请号:FR9816693

    申请日:1998-12-28

    Abstract: The invention concerns the upgrading of a by-product of direct synthesis, namely MeSiCl3, by vapor phase catalytic hydrogenation of said by-product to obtain MeHSiCl2 with greater added value. The invention concerns a method for preparing MeHSiCl2 by catalytic hydrogenation of MeSiCl3 in the presence of a metal catalyst with high selectivity levels in MeHSiCl2 economically and without having recourse to drastic and industrially unsuitable conditions. The invention uses a catalyst comprising a bimetal ruthenium/tin catalytic agent. Said catalytic agent is obtained by reacting ruthenium chloride and tin chloride in an acid medium. In practice, the catalyst is formed by a silica powder support impregnated by the ruthenium/tin catalytic agent.

    СПОСІБ ОДЕРЖАННЯ ЦИКЛОГЕКСАНОНУ

    公开(公告)号:UA83597C2

    公开(公告)日:2008-07-25

    申请号:UAA200706285

    申请日:2005-11-30

    Abstract: Данийвинахідстосуєтьсяспособуодержанняциклогексанонуз циклогексану. Детальнішевінстосуєтьсяспособуодержанняциклогексанону, щомаєнизькийвмістзабруднень, якийдозволяєзастосуванняциклогексанонуяквихідногоматеріалудляодержання (-капролактаму. Спосібзавинаходомвключаєобробкусумішіциклогексанолу/циклогексанону, одержаноїшляхомокисленнякиснемциклогексанунастадіїдегідрогенізаціїдляперетворенняциклогексанолунациклогексанон. Спосібзавинаходомпридатнийдляодержанняциклогексанонуз високимступенемчистоти, суміснимз йогозастосуваннямяквихідногоматеріалудлясинтезу (-капролактаму.

    PROCEDE DE PREPARATION DE CYCLOHEXANONE

    公开(公告)号:FR2878847A1

    公开(公告)日:2006-06-09

    申请号:FR0412976

    申请日:2004-12-07

    Abstract: Elle concerne plus particulièrement un procédé de préparation de cyclohexanone présentant une teneur en impuretés permettant une utilisation de la cyclohexanone comme matière première pour la fabrication d'ε-caprolactame.Le procédé de l'invention comprend notamment un traitement du mélange cyclohexanol/cyclohexanone issu de l'oxydation par l'oxygène du cyclohexane dans une étape de déshydrogénation pour transformer le cyclohexanol en cyclohexanone et les impuretés présentes telles que le cyclopentènal. Le procédé de l'invention permet d'obtenir une cyclohexanone présentant un degré de pureté élevé, compatible pour son utilisation comme matière première dans la synthèse de l'ε-caprolactame.

    7.
    发明专利
    未知

    公开(公告)号:FR2777006B1

    公开(公告)日:2000-08-04

    申请号:FR9804600

    申请日:1998-04-07

    Abstract: The invention concerns a method for preparing hydrogenated alkylmonosilanes, by catalytic hydrogenolysis, under hydrogen pressure, of halogenoorganopolysilanes, improving known methods, in particular by facilitating implementation, and in terms of cost-effectiveness and performance which are shown by the efficiency of the resulting hydrogenated monosilanes. In said method the starting polysilanes are of the type: (CH3)Cl2Si-SiCl(CH3)2; (CH3)Cl2Si-SiCl2(CH3); (CH3)Cl2Si-Si(CH3)3; (CH3)2ClSi-SiCl(CH3)2; (CH3)Cl2Si-SiCl(Ch3)-SiCl2(CH3); (CH3)Cl2Si-Si(CH3)(SiCH3Cl2)-SiCl2CH3. The hydrogenated monosilanes CH3H2ClSi; (CH3)2HClSi; CH3HCl2Si are obtained by contacting said polysilanes with gaseous hydrogen under pressure, in the presence of a catalytic system AB comprising a hydrogenation catalyst precursor A and an auxiliary B for dissolving precursor A in the reaction medium. Said catalytic system is further characterized in that it is reductant-free.

    8.
    发明专利
    未知

    公开(公告)号:FR2777006A1

    公开(公告)日:1999-10-08

    申请号:FR9804600

    申请日:1998-04-07

    Abstract: The invention concerns a method for preparing hydrogenated alkylmonosilanes, by catalytic hydrogenolysis, under hydrogen pressure, of halogenoorganopolysilanes, improving known methods, in particular by facilitating implementation, and in terms of cost-effectiveness and performance which are shown by the efficiency of the resulting hydrogenated monosilanes. In said method the starting polysilanes are of the type: (CH3)Cl2Si-SiCl(CH3)2; (CH3)Cl2Si-SiCl2(CH3); (CH3)Cl2Si-Si(CH3)3; (CH3)2ClSi-SiCl(CH3)2; (CH3)Cl2Si-SiCl(CH3)-SiCl2(CH3); (CH3)Cl2Si-Si(CH3)(SiCH3Cl2)-SiCl2CH3. The hydrogenated monosilanes CH3H2ClSi; (CH3)2HClSi; CH3HCl2Si are obtained by contacting said polysilanes with gaseous hydrogen under pressure, in the presence of a catalytic system AB comprising a hydrogenation catalyst precursor A and an auxiliary B for dissolving precursor A in the reaction medium. Said catalytic system is further characterised in that it is reductant-free.

    9.
    发明专利
    未知

    公开(公告)号:AT239027T

    公开(公告)日:2003-05-15

    申请号:AT99959503

    申请日:1999-12-21

    Abstract: The invention concerns the upgrading of a by-product of direct synthesis, namely MeSiCl3, by vapor phase catalytic hydrogenation of said by-product to obtain MeHSiCl2 with greater added value. The invention concerns a method for preparing MeHSiCl2 by catalytic hydrogenation of MeSiCl3 in the presence of a metal catalyst with high selectivity levels in MeHSiCl2 economically and without having recourse to drastic and industrially unsuitable conditions. The invention uses a catalyst comprising a bimetal ruthenium/tin catalytic agent. Said catalytic agent is obtained by reacting ruthenium chloride and tin chloride in an acid medium. In practice, the catalyst is formed by a silica powder support impregnated by the ruthenium/tin catalytic agent.

    PROCEDIMIENTO DE PREPARACION DE CICLOHEXANONA.

    公开(公告)号:ES2353236T3

    公开(公告)日:2011-02-28

    申请号:ES05822993

    申请日:2005-11-30

    Abstract: Un procedimiento de fabricación de ciclohexanona, caracterizado porque comprende las etapas siguientes: - Oxidar la ciclohexanona a hidroperóxido de ciclohexilo por medio de oxígeno en ausencia de catalizador - Purificar el medio de reacción mediante lavado con agua - Descomponer el hidroperóxido de ciclohexilo en ciclohexanol y ciclohexanona en presencia de un catalizador - Recuperar la mezcla ciclohexanol/ciclohexanona por separación del ciclohexano que no ha reaccionado y separación de los productos de punto de ebullición más elevado que los del ciclohexanol/ciclohexanona- Deshidrogenar el ciclohexanol contenido en la mezcla ciclohexanol/ciclohexanona en presencia de un catalizador de deshidrogenación- Destilar, en una primera etapa de destilación, la mezcla obtenida para obtener una fracción de cabeza (F1), que comprende los compuestos de punto de ebullición inferior a la temperatura de ebullición de la ciclohexanona, y una fracción de cola (Q1)- Destilar, en una segunda etapa de destilación, la fracción de cola (Q1) para obtener una fracción de cabeza (F2), constituida por la ciclohexanona, y una fracción de cola (Q2)

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