Process for the preparation of N-(ortho-alkylphenyl)-imides
    3.
    发明授权
    Process for the preparation of N-(ortho-alkylphenyl)-imides 失效
    制备N-(邻 - 烷基苯基) - 酰亚胺的方法

    公开(公告)号:US5684163A

    公开(公告)日:1997-11-04

    申请号:US595463

    申请日:1996-02-05

    CPC分类号: C07D207/452 C07D207/40

    摘要: A process for the preparation of a N-)ortho-alkylphenyl)-imide of the formula ##STR1## in which R.sup.1 to R.sup.9 is defined in the specification which comprises reacting a cyclic anhydride of the formula ##STR2## wherein R.sup.6 to R.sup.9 are difined in the specification with an amine of the formula ##STR3## optionally in the presence of an acid catalyst and optionally in the presence of a solvent which is immiscible or only slightly miscible with water but can form an azeotrope with water, at a temperature between 100.degree. to 200.degree. C. under conditions so that the water formed during the reaction is removed from the reaction mixture without the addition of a polymerization inhibitor or a dipolar solvent. The final products are used as intermediates to prepare heat-stable plastics as well as intermediates to prepare pharmaceutical and agricultural chemicals.

    摘要翻译: 制备式(I)的N-)邻 - 烷基苯基) - 酰亚胺的方法,其中R 1至R 9在本说明书中定义,其包括使下式的环状酸酐(II) 其中R6至R9在本说明书中与式(III)的胺任选在酸催化剂存在下,任选在与水不混溶或仅与水轻微混溶的溶剂存在下, 与水共沸,在100至200℃的温度条件下,使得在反应期间形成的水从反应混合物中除去而不加入阻聚剂或偶极溶剂。 最终产品用作制备热稳定塑料的中间体以及制备药物和农药的中间体。

    Process for the preparation of dinitro-polyalkylbenzenes
    4.
    发明授权
    Process for the preparation of dinitro-polyalkylbenzenes 失效
    二硝基 - 多烷基苯的制备方法

    公开(公告)号:US5367108A

    公开(公告)日:1994-11-22

    申请号:US80026

    申请日:1993-06-18

    CPC分类号: C07C201/08

    摘要: Dinitro-polyalkylbenzenes can be prepared by nitration of polyalkylbenzenes using HNO.sub.3 in the presence of H.sub.2 SO.sub.4 in such a manner that at least 50% of the H.sub.2 SO.sub.4 is present as reaction medium and HNO.sub.3 and the polyalkylbenzene and any remaining H.sub.2 SO.sub.4 are added simultaneously in such a manner that the added substances polyalkylbenzene and HNO.sub.3 are in the molar ratio of 1:2-10. H.sub.2 SO.sub.4 is used at a concentration from 81 to 96% by weight and HNO.sub.3 at a concentration from 95 to 100% by weight. For the work-up, the dinitro-polyalkylbenzenes are first freed from the majority of the acids and then treated with a highly dilute aqueous solution of a dispersant for separating off residual acid.

    摘要翻译: 二硝基 - 聚烷基苯可以通过在H 2 SO 4的存在下使用HNO 3硝化多烷基苯来制备,使得至少50%的H 2 SO 4作为反应介质存在,并且以这种方式同时加入HNO 3和多烷基苯以及任何剩余的H 2 SO 4 所添加的物质聚烷基苯和HNO 3的摩尔比为1:2-10。 使用浓度为81至96重量%的H 2 SO 4,浓度为95至100重量%的HNO 3。 对于后处理,二硝基聚烷基苯首先从大多数酸中脱除,然后用高度稀释的用于分离残余酸的分散剂的水溶液处理。

    Process for the adiabatic preparation of mononitrohalogenobenzenes
    6.
    发明授权
    Process for the adiabatic preparation of mononitrohalogenobenzenes 失效
    绝热制备单硝基卤代苯的工艺

    公开(公告)号:US5714647A

    公开(公告)日:1998-02-03

    申请号:US785577

    申请日:1997-01-21

    CPC分类号: C07C201/08

    摘要: Mononitrohalogenobenzenes can be prepared by mixing halogenobenzene, nitric acid, sulphuric acid and water intensively with one another, simultaneously or in succession in their total quantity, and by redispersing them at least twice in the case of continuous preparation, applying a mixing energy of 1-40 watts per liter of the overall reaction mixture, preferably 3-30 W/l, largely suppressing back-mixing in the continuous procedure, and observing adiabatic reaction conditions.

    摘要翻译: 一硝基卤代苯可以通过将卤代苯,硝酸,硫酸和水彼此同时或相继地以总量相互重叠混合,并且在连续制备的情况下将它们再分散至少两次来制备, 总体反应混合物为40瓦/升,优选为3-30W / l,在连续方法中大大抑制了反混合,并且观察绝热反应条件。

    Process for the adiabatic preparation of mononitrotoluenes
    7.
    发明授权
    Process for the adiabatic preparation of mononitrotoluenes 失效
    制备单硝基甲苯的绝热方法

    公开(公告)号:US5648565A

    公开(公告)日:1997-07-15

    申请号:US679323

    申请日:1996-07-12

    CPC分类号: C07C201/08

    摘要: Mononitrotoluenes can be prepared by intensively mixing together toluene, nitric acid, sulphuric acid and water, simultaneously or successively in their total amount, and, in the case of continuous preparation, redispersing the mixture at least twice, for which purpose a mixing energy of 1 to 40 watts per liter of the total reaction mixture, preferably 3 to 30 W/l, is employed per volume of the reactor, and, for the continuous procedure, the back mixing is substantially repressed. Adiabatic reaction conditions are maintained.

    摘要翻译: 单硝基甲苯可以通过将甲苯,硝酸,硫酸和水同时或相继浓缩在一起而制备,并且在连续制备的情况下,将混合物再分散至少两次,为此目的的混合能量为1 至40瓦/升的总反应混合物,优选3至30W / l,并​​且对于连续方法,背混合基本上被压制。 保持绝热反应条件。