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    • 4. 发明专利
    • BR8606411A
    • 1987-10-13
    • BR8606411
    • 1986-12-23
    • KARL LOHRBERG
    • LOHRBERG KARL
    • B01D3/20B01J10/00C01B11/02
    • Chlorine dioxide is increasibly used to bleach pulp and the like. Chlorine dioxide is produced in a reactor, which contains a plurality of superimposed bubble cap trays, which are provided with passages for the gas and with duct, which is independent of the gas passages and serves as an overflow for the liquid. In order to maintain a maximum ClO3/acid ratio for the longest time possible, the reaction chamber above each bubble cap tray is divided into a large number of reaction compartments by vertical partitions, which define openings for the passage of the reaction liquid. Acid can be supplied to each compartment. The partitions can be used to define in each reaction chamber any desired number of reaction compartments, which are connected in parallel for the flow of acid and are connected in series for the flow of the chlorate solution.
    • 6. 发明授权
    • Process for producing alkali hydroxide, chlorine and hydrogen by the
electrolysis of an aqueous alkali chloride solution in a membrane cell
    • 通过在膜电池中电解碱性氯化碱水溶液来生产碱金属氢氧化物,氯和氢的方法
    • US4839003A
    • 1989-06-13
    • US116433
    • 1987-11-03
    • Rainer DworakKarl Lohrberg
    • Rainer DworakKarl Lohrberg
    • C01D3/16C25B1/46C25B15/08
    • C25B15/08C01D3/16
    • Alkali hydroxide, chlorine and hydrogen are produced from an aqueous alkali chloride solution by membrane electrolysis. A high-NaCl solid salt, which contains impurities, is dissolved in water in a salt dissolver. Precipitating chemicals are added to the salt solution to precipitate the impurities. The resulting mixture is fed to a thickener, from which precipitates and clarified raw brine are separately withdrawn. The clarified raw brine from the thickener is divided at a ratio between 2:1 and 20:1 into first and second partial streams. The larger first partial stream is mixed with the salt solution and the precipitating chemicals before entering the thickener and the resulting mixture is fed to the thickener. The second partial stream of the clarified raw brine is fed through a fine purifier to the electrolytic cell. Spent brine from the electrolytic cell is fed to the salt dissolver.
    • 通过膜电解由氯化碱水溶液制备氢氧化碱,氯和氢。 将含有杂质的高NaCl固体盐溶解在盐溶解器中的水中。 将沉淀的化学品加入到盐溶液中以沉淀杂质。 将所得混合物加入到增稠剂中,从中分离出沉淀物和澄清的生盐水。 来自增稠剂的澄清的原料盐水以2:1至20:1的比例分成第一和第二部分流。 在进入增稠剂之前,较大的第一部分流与盐溶液和沉淀化学品混合,并将所得混合物进料至增稠剂。 澄清的生盐水的第二部分流通过细小的净化器送入电解池。 将来自电解池的废水进料到盐溶解器中。
    • 10. 发明授权
    • Method of and reactor for producing chlorine dioxide
    • 生产二氧化氯的方法和反应器
    • US4938944A
    • 1990-07-03
    • US361036
    • 1989-06-02
    • Rainer DworakPeter KohlKarl LohrbergReinhard Muller
    • Rainer DworakPeter KohlKarl LohrbergReinhard Muller
    • C01B11/02
    • C01B11/025B01J14/00B01J19/245B01J2219/00083
    • For the production of a gaseous mixture contains chlorine dioxide and chlorine, alkali chlorate in an aqueous solution with acid is reacted in a reactor. The reactor comprises a plurality of superimposed reaction levels which are traversed by the solution from top to bottom. In the lower portion of the reactor the solution in which chlorate and acid have been depleted is reboiled in a reboiling chamber by an indirect heating at a temperature in the range from 100.degree. to 110.degree. C. The depleted solution is conducted from the reboiling chamber to a pressure chamber, in which a pressure of at least 1.2 bar is maintained. In the pressure chamber the solution is reboiled at temperatures from 110.degree. to 150.degree. C. and the vapors formed by the reboiling in the pressure chamber are conducted through the reboiling chamber for an indirect heating therein.
    • 为了生产含有二氧化氯和氯的气态混合物,在酸的水溶液中的氯酸碱在反应器中反应。 反应器包括多个叠加的反应水平,其通过溶液从上到下穿过。 在反应器的下部,其中氯酸盐和酸已经耗尽的溶液通过在100-110℃的温度下间接加热在再沸室中再沸腾。贫化溶液从再沸室 到压力室,其中保持至少1.2巴的压力。 在压力室中,溶液在110℃至150℃的温度下再沸腾,通过再沸器形成的蒸气通过再沸腾室进行间接加热。