Process and reaction vessel for production of alkyl nitrite
    91.
    发明公开
    Process and reaction vessel for production of alkyl nitrite 无效
    用于生产亚硝酸盐的工艺和反应容器

    公开(公告)号:EP0310191A3

    公开(公告)日:1990-12-12

    申请号:EP88202116.5

    申请日:1988-09-28

    CPC classification number: B01D3/009 C07C201/04 Y02P20/127 C07C203/00

    Abstract: A process and reaction vessel for producing alkyl nitrite is disclosed, the process comprising (a) contacting nitric oxide¸ lower alcohol and oxygen in a reaction zone such that alkyl nitrite is formed, said reaction zone comprising a reactor section and a rectification section, (b) supplying a liquid scrubbing agent to an upper portion of the rectification section, (c) withdrawing a gaseous alkyl nitrite product stream from the upper portion of the rectification section, and (d) withdrawing a liquid stream from a lower portion of the reactor section. The reactor section provides intimate vapor-liquid contact sufficient to enhance the conver­sion of nitric oxide to alkyl nitrite and the rectification section provides sufficient vapor residence time to enhance conversion of oxygen, as well as sufficient rectification capabilities to reduce the amounts of water and nitric acid in the gaseous alkyl nitrite product stream.

    Process and reaction vessel for production of alkyl nitrite
    93.
    发明公开
    Process and reaction vessel for production of alkyl nitrite 无效
    Verfahren undReaktionsgefässzur Herstellung von Alkylnitrit。

    公开(公告)号:EP0310191A2

    公开(公告)日:1989-04-05

    申请号:EP88202116.5

    申请日:1988-09-28

    CPC classification number: B01D3/009 C07C201/04 Y02P20/127 C07C203/00

    Abstract: A process and reaction vessel for producing alkyl nitrite is disclosed, the process comprising (a) contacting nitric oxide¸ lower alcohol and oxygen in a reaction zone such that alkyl nitrite is formed, said reaction zone comprising a reactor section and a rectification section, (b) supplying a liquid scrubbing agent to an upper portion of the rectification section, (c) withdrawing a gaseous alkyl nitrite product stream from the upper portion of the rectification section, and (d) withdrawing a liquid stream from a lower portion of the reactor section. The reactor section provides intimate vapor-liquid contact sufficient to enhance the conver­sion of nitric oxide to alkyl nitrite and the rectification section provides sufficient vapor residence time to enhance conversion of oxygen, as well as sufficient rectification capabilities to reduce the amounts of water and nitric acid in the gaseous alkyl nitrite product stream.

    Abstract translation: 公开了一种用于生产亚硝酸烷基酯的方法和反应容器,该方法包括(a)在反应区中使一氧化氮和己二醇与低级醇与氧接触,从而形成亚硝酸烷基酯,所述反应区包括反应器部分和精馏段( b)将液体洗涤剂供应到精馏段的上部,(c)从精馏段的上部排出气态烷基亚硝酸盐产物流,和(d)从反应器的下部排出液体物流 部分。 反应器部分提供充分的气液接触,足以增强一氧化氮向亚硝酸烷基酯的转化,并且精馏段提供足够的蒸气停留时间,以提高氧气的转化率,以及足够的整流能力以减少水和硝酸的量 在气态烷基亚硝酸盐产物流中。

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