Process and reaction vessel for production of alkyl nitrite
    121.
    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。

    C1- C4- 알킬아 질산염의 제조 방법
    124.
    发明公开
    C1- C4- 알킬아 질산염의 제조 방법 无效
    生产硝酸C1-C4-烷基酯的方法

    公开(公告)号:KR1019940021514A

    公开(公告)日:1994-10-19

    申请号:KR1019940004423

    申请日:1994-03-08

    CPC classification number: C07C201/04 C07C203/00

    Abstract: C-C-알킬아질산염은, 삼산화이질소로서의질소산화물즉, a) 그자체로서, b) 일산화질소와의혼합물로서, 또는 c) 이의전구체인일산화탄소/이산화질소또는일산화탄소/사산화이질소의혼합물로서반응기하부에서사용함을특징으로하여, 스크러버컬럼으로서설계된반응기내에서산소의관여없이 C-C-알칸올을질소산화물과반응시킴으로써제조할수 있다. 한편사용된 C-C-알칸올의총 양중 5 내지 60%가기화또는분무형태로반응기의하부내에서사용되는반면, 나머지 C-C-알칸올은컬럼상부로이동된다.

    Abstract translation: CC-亚硝酸烷基酯,氮氧化物即,)本身作为化二氮,B)与一氧化氮的混合物或c)它们的一氧化碳/氮气二氧化碳或一氧化碳的前体的混合物/四氧化二氮在反应器的底部启用 其特征在于,没有氧气的在设计为洗涤塔的反应器中的参与的一个,CC-烷醇,它可以通过与NOx反应而制备。 在另一方面,而具有总抬起使用在反应器的下部用于喷雾或丝网形式的顶部,其余C-C-链烷醇的C-C-烷醇5%至60%被移动到塔顶。

    Process for producing C1-C4 alkyl nitrite
    129.
    发明授权
    Process for producing C1-C4 alkyl nitrite 有权
    制备C1-C4烷基亚硝酸盐的方法

    公开(公告)号:US08476469B2

    公开(公告)日:2013-07-02

    申请号:US13087285

    申请日:2011-04-14

    CPC classification number: C07C201/04 C07C203/00

    Abstract: A process of producing C1-C4 alkyl nitrite, comprising the following steps: a) firstly feeding nitrogen oxide and oxygen into Reactor I, contacting with an aluminosilicate catalyst, and reacting to produce an effluent I containing NO2 and unreacted NO; b) feeding the effluent I and C1-C4 alkanol into Reactor II, and reacting to produce an effluent II containing C1-C4 alkyl nitrite; and c) separating the effluent II containing C1-C4 alkyl nitrite to obtain C1-C4 alkyl nitrite; wherein reactor I is a fixed bed reactor, and Reactor II is a rotating high-gravity reactor; said nitrogen oxide in step a) is NO, or a mixed gas containing NO and one or more of N2O3 and NO2, wherein the molar number of NO is greater than that of NO2, if any; and the molar ratio of NO in nitrogen oxide to oxygen is 4-25:1.

    Abstract translation: 一种生产C1-C4烷基亚硝酸盐的方法,包括以下步骤:a)首先将氮氧化物和氧气加入到反应器I中,与铝硅酸盐催化剂接触,并产生含有NO 2和未反应的NO的流出物I; b)将流出物I和C 1 -C 4烷醇加入到反应器II中,并产生含有亚硝酸C1-C4烷基酯的流出物II; 和c)分离含有C1-C4烷基亚硝酸盐的流出物II,得到亚硝酸C1-C4烷基酯; 其中反应器I是固定床反应器,反应器II是旋转的高重力反应器; 步骤a)中的氮氧化物为NO,或含有NO和一种或多种N 2 O 3和NO 2的混合气体,其中NO的摩尔数大于NO 2的摩尔数(如果有的话)。 氮氧化物中的NO与氧的摩尔比为4-25:1。

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