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    • 1. 发明授权
    • Process for the production of dinitrotoluene
    • 生产二硝基甲苯的方法
    • US07041858B1
    • 2006-05-09
    • US11054012
    • 2005-02-09
    • Juergen MuennigBernd PennemannDietmar WastianVolker MicheleJesse CaravaggioJohn F. Gisch, Jr.
    • Juergen MuennigBernd PennemannDietmar WastianVolker MicheleJesse CaravaggioJohn F. Gisch, Jr.
    • C07C205/00
    • C07C201/08C07C205/06
    • The present invention is directed to a process for the isothermal nitration of aromatic organic compounds, wherein an aromatic organic compound is brought into contact and reacted with a mixture of sulfuric acid and nitric acid. The mixture of sulfuric acid and nitric acid, and the aromatic organic compound are brought into contact with each other through a mixing nozzle which comprises a substantially cylindrical tubular reactor and an annular gap which surrounds the tubular reactor. The aromatic organic compound flows through the tubular reactor, and the mixture of sulfuric acid and nitric acid flows through the annular gap, and they are mixed together upon emerging from the tubular reactor and the annular gap, wherein the ratio of the average rates of flow of the aromatic organic compound in the tubular reactor, and of the mixture of sulphuric acid and nitric acid in the annular gap ranges from 0.5:1 to 10:1.
    • 本发明涉及芳族有机化合物的等温硝化方法,其中使芳族有机化合物与硫酸和硝酸的混合物接触并反应。 硫酸和硝酸的混合物和芳香族有机化合物通过混合喷嘴相互接触,所述混合喷嘴包括基本上圆柱形的管式反应器和围绕管状反应器的环形间隙。 芳族有机化合物流过管状反应器,硫酸和硝酸的混合物流过环形间隙,并且在从管式反应器和环形间隙出现时将它们混合在一起,其中平均流速 的管状反应器中的芳族有机化合物,以及环状间隙中的硫酸和硝酸的混合物的范围为0.5:1至10:1。