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    • 5. 发明授权
    • Process for purifying and concentrating spent sulfuric acids
    • 净化和浓缩废硫酸的方法
    • US6156288A
    • 2000-12-05
    • US205672
    • 1998-12-04
    • Heiko BeckhausJurgen MunnigDieter Grenner
    • Heiko BeckhausJurgen MunnigDieter Grenner
    • C01B17/88C01B17/90C01B17/94
    • C01B17/94C01B17/88C01B17/90
    • A process is provided for the purification of sulfuric acid contaminated with impurities, such as nitric acid, nitrosylsulfuric acid, dinitrotoluenes and mononitrotoluenes, wherein this contaminated sulfuric acid was obtained from the production of nitrated toluene using toluene and nitric acid. The contaminated sulfuric acid is preheated to a temperature in the range of 50 to 180.degree. C. in a heat exchanger. The heated, contaminated sulfuric acid is freed from steam-volatile impurities, such as dinitrotoluenes and mononitrotoluenes, and the nitrogen-containing compounds within the sulfuric acid are decomposed by counter currently contacting the contaminated sulfuric acid with steam and vapors from a downstream concentration step in a steam stripper, which is operated at a pressure ranging from 300 to 1,000 mbars. The steam-stripped sulfuric acid is fed into a first concentration stage, which is operated at the same pressure used in the steam stripper. The concentrated sulfur acid is then fed into a vacuum concentration process which produces a sulfuric acid having a concentration of 88 to 97 percent by weight. By using the same pressure that the steam stripper operates at in the first concentration stage, the crystallization of nitroaromatic compounds can be avoided in the condensation system of the concentration stages, along with the concomitant blockage of the condensation system that would have been caused by the crystals.
    • 提供了用于净化被杂质污染的硫酸的方法,例如硝酸,亚硝酰基硫酸,二硝基甲苯和一硝基甲苯,其中该受污染的硫酸是使用甲苯和硝酸从硝化甲苯生产得到的。 将污染的硫酸在热交换器中预热至50〜180℃的温度。 受热污染的硫酸不含蒸汽挥发性杂质,例如二硝基甲苯和单硝基甲苯,硫酸中的含氮化合物由目前与污染的硫酸接触的蒸汽和蒸汽从下游浓缩步骤中分解 蒸汽汽提器,其工作压力范围为300至1,000千巴。 将蒸汽汽提的硫酸进料到第一浓缩阶段,其在与汽提塔中相同的压力下运行。 然后将浓硫酸加入到产生浓度为88-97重量%的硫酸的真空浓缩过程中。 通过使用蒸汽汽提器在第一浓缩阶段中操作的相同压力,在浓缩阶段的冷凝系统中可以避免硝基芳族化合物的结晶,同时伴随着会引起凝结系统的堵塞 晶体。