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non continuous two-stage chlorination methods for the production of neutral calciumhypochlorit advantage.

机译:非连续两阶段氯化法生产中性次氯酸钙的优势。

摘要

1. Discontinuous process for the preparation of neutral calcium hypochlorite hydrate, in the form of an aqueous slurry, according to which gaseous chlorine is reacted, in two chlorination stages, with an aqueous slurry with a calcium hydroxide content of 160 to 360 g/l and the reaction medium is kept stirred, characterized by the fact that, in the first step, a chlorination operation is effected at a temperature below 40 degrees C and preferably of between 20 and 35 degrees C, and continued until the calcium hydroxide content of the reaction medium has been lowered to between 45 and 80 g/l, the temperature of the reaction medium is lowered to between 0 and 12 degrees C in less than 30 minutes and preferably less than 20 minutes and, in the second step, a chlorination operation is then effected at a temperature of between 5 and 22.5 degrees C, the rate of flow of chlorine being regulated in such a way that the duration of the said chlorination operation, necessary to lower the calcium hydroxide content of the reaction medium to below 16 g/l and preferably between 5 and 10 g/l, is between 10 and 25 minutes, and the temperature of the reaction medium is lowered to or maintained at below 20 degrees C and preferably between 12 and 15 degrees C, the maximum temperatures theta 1 and theta 2 reached in the course of, respectively, the first and the second steps being such that the difference theta 1 -theta 2 is at least equal to 15 degrees C, and that it is applied to calcium hydroxide in the form of particles with a diameter of between 0 and 200 mu m.
机译:1.不连续的制备水浆形式的中性次氯酸钙水合物的方法,根据该过程,气态氯在两个氯化阶段中与氢氧化钙含量为160至360 g / l的水浆反应使反应介质保持搅拌,其特征在于,在第一步中,氯化操作是在低于40摄氏度,最好是20到35摄氏度的温度下进行的,并持续进行到氯化氢的氢氧化钙含量为止。将反应介质的温度降低到45至80 g / l之间,在不到30分钟,最好是不到20分钟的时间内将反应介质的温度降低到0至12摄氏度,并且在第二步中进行氯化操作然后在5至22.5℃之间的温度下进行氯化,以这样的方式调节氯的流速,使得降低氯化钙的h所需的所述氯化操作的持续时间。反应介质中的氧化物含量低于16 g / l,优选5至10 g / l,介于10至25分钟之间,反应介质的温度降低至或保持在20摄氏度以下,优选12至12摄氏度之间。在温度为15摄氏度时,在第一步和第二步过程中分别达到的最高温度theta 1和theta 2使得相差theta 1 -theta 2至少等于15摄氏度,并且以直径为0至200微米的颗粒形式应用于氢氧化钙。

著录项

  • 公开/公告号AT45715T

    专利类型

  • 公开/公告日1989-09-15

    原文格式PDF

  • 申请/专利权人 ATOCHEM;

    申请/专利号AT19860401447T

  • 发明设计人 GUERIN JEAN;

    申请日1986-06-30

  • 分类号C01B11/06;

  • 国家 AT

  • 入库时间 2022-08-22 06:36:58

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