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    • 2. 发明授权
    • Process for the production of dinitrotoluene
    • 生产二硝基甲苯的方法
    • US5679873A
    • 1997-10-21
    • US510992
    • 1995-08-03
    • Uwe KlinglerThomas SchiebGerhard WiechersJurgen Zimmermann
    • Uwe KlinglerThomas SchiebGerhard WiechersJurgen Zimmermann
    • C07C201/08C07C201/16C07C205/06
    • C07C201/08
    • Dinitrotoluene is produced in a two-stage process from toluene and nitric acid in the presence of sulfuric acid under adiabatic conditions in the presence of nitrating acids made up of specified components. The reaction product of the first phase is separated into an acid phase and an organic phase containing the mononitrotoluene. Some water is removed from the acid phase, nitric acid is added and the resultant mixture is recycled. The organic phase containing mononitrotoluene is further nitrated to produce the dinitrotoluene. This nitration mixture is also separated into an acid phase and an organic phase. The acid phase is treated to remove some water, nitric acid is added and the resultant acid mixture is recycled. Dinitrotoluene is recovered from the organic phase. This process is advantageous in that dilute nitric acid may be used and the heat of the nitration reaction is utilized.
    • 在绝酸条件下,在由特定组分组成的硝酸的存在下,在硫酸存在下,甲苯和硝酸二步法生产二硝基甲苯。 将第一相的反应产物分离成酸相和含有一硝基甲苯的有机相。 从酸相中除去一些水,加入硝酸并将所得混合物回收。 含有单硝基甲苯的有机相进一步硝化以产生二硝基甲苯。 该硝化混合物也分离成酸相和有机相。 处理酸相以除去一些水,加入硝酸并将所得酸混合物再循环。 从有机相回收二硝基甲苯。 该方法的优点在于可以使用稀硝酸并利用硝化反应的热。
    • 5. 发明授权
    • Process for the production of nitroaromatic compounds
    • 制备硝基芳族化合物的方法
    • US5696305A
    • 1997-12-09
    • US510888
    • 1995-08-03
    • Uwe KlinglerThomas SchiebGerhard WiechersJurgen Zimmermann
    • Uwe KlinglerThomas SchiebGerhard WiechersJurgen Zimmermann
    • C07C201/08C07C205/06C07C205/12
    • C07C201/08
    • Nitroaromatic compounds are produced by continuously reacting an aromatic compound with nitrating acid. The reaction mixture is separated into an organic phase from which the desired nitroaromatic compound is recovered and an acid phase. The acid phase is subjected to flash evaporation to remove at least 5% by weight of the water present therein. The vapors generated during the flash evaporation are introduced into a jet spray of coolant to produce a condensate made up coolant, condensed vapors and suspended organic compounds. A portion of the condensate is subjected to phase separation to remove water and organic compounds present therein. The water and organic compounds may be reused. The process of the present invention is particularly advantageous in that deposits which block pipelines and interfere with heat transfer are not generated.
    • 硝基芳族化合物是通过使芳族化合物与硝酸进行连续反应来制备的。 将反应混合物分离成有机相,从中回收所需的硝基芳族化合物和酸相。 将酸相进行闪蒸以除去其中存在的至少5重量%的水。 在闪蒸期间产生的蒸汽被引入冷却剂的喷射喷雾中以产生冷却剂,冷凝蒸汽和悬浮的有机化合物的冷凝物。 将一部分冷凝物进行相分离以除去其中存在的水和有机化合物。 水和有机化合物可以重复使用。 本发明的方法特别有利的是不产生堵塞管道并干扰热传递的沉积物。
    • 6. 发明授权
    • Process for the production of dinitrotoluene and isomeric mixtures of
dinitrotoluene
    • 制备二硝基甲苯和二硝基甲苯异构体混合物的方法
    • US5663462A
    • 1997-09-02
    • US657513
    • 1996-06-04
    • Uwe KlinglerThomas SchiebGerhard Wiechers
    • Uwe KlinglerThomas SchiebGerhard Wiechers
    • C07C201/08C07C201/16C07C205/06
    • C07C201/08
    • Dinitrotoluene and isomer mixtures of dinitrotoluene are produced in a single stage, continuous process by nitrating mononitrotoluene or an isomer mixture of mononitrotoluene in which the ortho-mononitrotoluene content is low with a nitrating acid made up of (1) from about 80 to about 100 wt. % inorganic constituents and (2) up to 20 wt. % organic constituents. The inorganic constituents of the nitrating acid include: (a) from about 60 to about 90 wt. % sulfuric acid, (b) from about 1 to about 20 wt. % nitric acid, and (c) at least 5 wt. % water. The organic constituents of the nitrating acid include: from about 70 to about 100% by weight nitrotoluene isomers and up to about 30% by weight nitration by-products. The nitration reaction is carrier out under adiabatic conditions. The molar ratio of nitric acid to mononitrotoluene during the nitration reaction is generally from about 0.7:1 to about 1.4:1. The phases generated during the nitration are subsequently separated and the acid phase is treated to remove at least 5 wt. % of the water present therein. The water may be removed by distillation or flash vaporization, optionally with simultaneous heat supply. After removal of the water, nitric acid having a concentration of from about 50 to about 100 wt. % is added to the treated acid phase in amount sufficient to satisfy the compositional limits for a nitrating acid useful in the process of the present invention. This reconcentrated acid phase is then returned to the nitration reaction.
    • 二硝基甲苯和二硝基甲苯的异构体混合物通过硝化单硝基甲苯或单硝基甲苯的异氰酸甲酯的异构体混合物在单一阶段中生产,其中邻硝基甲苯含量低于由(1)约80至约100重量% 。 %无机成分和(2)最多20重量% %有机成分。 硝酸的无机组分包括:(a)约60至约90wt。 %硫酸,(b)约1至约20wt。 %硝酸,和(c)至少5wt。 % 水。 硝酸的有机成分包括:约70至约100重量%的硝基甲苯异构体和至多约30重量%的硝化副产物。 硝化反应在绝热条件下载运。 在硝化反应期间硝酸与单硝基甲苯的摩尔比通常为约0.7:1至约1.4:1。 随后分离硝化过程中产生的相,并处理酸相以除去至少5wt。 存在于其中的水的百分比。 水可以通过蒸馏或闪蒸除去,任选地同时供热。 除去水后,浓度为约50至约100wt。 以足以满足本发明方法中有用的硝酸的组成限度的量将经加入的酸相中的%加入到处理的酸相中。 然后将该再浓缩的酸相返回到硝化反应。