亜硝酸エステルの製造方法、並びにシュウ酸ジアルキル及び炭酸ジアルキルの製造方法
    291.
    发明申请
    亜硝酸エステルの製造方法、並びにシュウ酸ジアルキル及び炭酸ジアルキルの製造方法 审中-公开
    生产硝酸酯的方法,以及生产二烷基氧化铝和碳酸二乙酯的方法

    公开(公告)号:WO2013150840A1

    公开(公告)日:2013-10-10

    申请号:PCT/JP2013/055148

    申请日:2013-02-27

    Abstract:  一酸化窒素と酸素とアルコールとを反応させて亜硝酸エステルを生成させる亜硝酸エステルの製造方法であって、上記反応塔の底部からの塔底液と、一酸化窒素及び/又は一酸化炭素とを反応器に供給して亜硝酸エステルを生成させる工程と、亜硝酸エステルを反応塔に供給する工程と、反応器から水と硝酸とアルコールとを含有する反応液を硝酸濃縮塔に供給する工程と、硝酸濃縮塔において、硝酸濃縮塔の底部に生じる濃縮液中のアルコール濃度を4.0重量%未満に制御しながら、反応液から低沸点分を蒸留分離して、硝酸濃縮塔の下部から、濃縮液を反応器に導入する工程と、を有する亜硝酸エステルの製造方法である。

    Abstract translation: 一种用于生产亚硝酸酯的方法,其中使一氧化氮,氧和醇反应以产生亚硝酸酯,所述产生亚硝酸酯的方法包括:从反应塔底部供应底部液体的步骤 ,和一氧化氮和/或一氧化碳转化成反应器以产生亚硝酸酯; 将亚硝酸酯供应到反应塔的步骤; 从反应器将含有水,硝酸和醇的反应液供给到硝酸浓缩塔的步骤; 以及通过蒸馏将低沸点馏分与反应液分离的步骤,同时控制硝酸浓缩塔底部产生的浓缩液中的醇浓度小于4.0重量%,将浓缩液引入反应器 。

    Method for producing c1-c4 alkyl nitrite
    294.
    发明专利
    Method for producing c1-c4 alkyl nitrite 有权
    生产C1-C4烷基硝酸盐的方法

    公开(公告)号:JP2011236209A

    公开(公告)日:2011-11-24

    申请号:JP2011090875

    申请日:2011-04-15

    CPC classification number: C07C201/04 C07C203/00

    Abstract: PROBLEM TO BE SOLVED: To provide a new method for producing C-Calkyl nitrite having advantage of high selectivity of C-Calkyl nitrite.SOLUTION: This method for producing C-Calkyl nitrite includes processes for: loading a resin catalyst layer and/or a porous filler layer into a reactor; passing nitrogen oxide, oxygen and C-Calcohol as raw materials through the resin catalyst layer and/or porous filler layer in a counter current, parallel current or cross current manner; and reacting under the reaction conditions including a reaction temperature of 0-150°C, a reaction pressure of -0.09 to 1.5 MPa, a molar ratio of C-Calkanol/nitrogen oxide of 1-100:1, a molar ratio of nitrogen oxide/oxygen of 4-50:1, to obtain waste liquid containing C-Calkyl nitrite; wherein the nitrogen oxide is NO, or a mixed gas containing NO and one or more selected from NOand NO.

    Abstract translation: 要解决的问题:提供一种新方法,用于生产具有优势的C 1 选择性C 1 -C 4 亚硝酸烷基酯。

    解决方案:用于生产C 1 -C 4 亚硝酸烷基酯的方法包括以下步骤:将树脂催化剂层和 /或多孔填料层进入反应器; 通过树脂催化剂层和/或多孔填料层作为原料通过氮氧化物,氧气和C 1 -C 4 以逆流,并联电流或交叉电流方式; 在反应温度0〜150℃,反应压力-0.09〜1.5MPa,摩尔比C 1 -C 4 链烷醇/氮氧化物为1-100:1,氮氧化物/氧气的摩尔比为4-50:1,得到含有C 1 -C 4 亚硝酸烷基酯; 其中氮氧化物为NO,或含有NO的混合气体和选自N 3 和NO < SB POS =“POST”> 2 。 版权所有(C)2012,JPO&INPIT

    METHOD FOR PRODUCING ALKYL NITRITE
    296.
    发明专利

    公开(公告)号:JP2003261515A

    公开(公告)日:2003-09-19

    申请号:JP2002060376

    申请日:2002-03-06

    Applicant: UBE INDUSTRIES

    Abstract: PROBLEM TO BE SOLVED: To provide a method for efficiently producing an alkyl nitrite in higher yield by reaction between nitrogen dioxide and an alkanol. SOLUTION: The method for producing the alkyl nitrite comprises feeding a reaction column with the alkanol and water to allow them to flow down and countercurrently contacting them with the nitrogen oxide while feeding it into the reaction column. More specifically, this method comprises the step (1) of introducing bottoms extracted from the bottom of the reaction column into a reactor, into which carbon monoxide or hydrogen is fed in the presence of a platinum metal catalyst and both the alkanol and nitric acid in the bottoms are reacted with the carbon monoxide or hydrogen to form the alkyl nitrite and the step (2) of feeding the alkyl nitrite into the zone where the alkanol in the reaction column is flowing down. COPYRIGHT: (C)2003,JPO

    METHOD FOR PREPARING ALKYL NITRITE
    297.
    发明专利

    公开(公告)号:JP2003128634A

    公开(公告)日:2003-05-08

    申请号:JP2001323123

    申请日:2001-10-22

    Applicant: UBE INDUSTRIES

    Abstract: PROBLEM TO BE SOLVED: To provide an industrially preferable method for preparing an alkyl nitrite which is capable of preparing the alkyl nitrite easily and at a low cosy with a high efficiency. SOLUTION: The method for preparing the alkyl nitrite is characterized by reacting nitric acid and an alkanol, in the presence of a platinum group metal catalyst, with carbon monoxide or hydrogen. Further, a method for preparing the alkyl nitrite is characterized by using an aqueous solution containing nitric acid wherein the concentration of nitric acid is not higher than 60% by weight and contains 5 to 70% by weight of an alkanol, in the presence of the solid catalyst in which the platinum group metal or its compound is supported on the carrier, and the reaction is conducted until the concentration of nitric acid reaches not higher than 1% by weight.

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