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A process for the recuperation of mercury from an inactive mercury - ii - chloride / activated carbon - contact

机译:从非活性汞中回收汞的方法-ii-氯化物/活性炭-接触

摘要

1,162,328. Recovery of mercury chlorides from catalysts. KNAPSACK A.G. 2 April, 1968 [4 April, 1967], No. 15742/68. Heading C1A. [Also in Division C7] In the recovery of Hg from a contaminated inactive HgCl 2 / active C catalyst by burning the C with a deficiency of O 2 or air so as to produce predominantly CO, a mixture consisting of gaseous Hg, HgCl 2 and Hg 2 Cl 2 is expelled or sublimed off (together with combustion gases), the mixture is condensed, and the HgCl 2 and Hg 2 Cl 2 in the condensate are reduced to Hg by addition of a reducing agent such as hydrazine sulphate, ferrous sulphate or formaldehyde. As shown, inactive catalyst 9 is burnt in shaft furnace 3. The products leave the furnace through line 10 and are cooled in tube condenser 11. Condensate and combustion gases pass through line 13 to scrubbing tower 14 which is supplied with reducing solution 15. Hg is withdrawn at 17, while combustion gases, after scrubbing out of mercury chloride contaminants and reduction thereof, leave through line 16 and are burnt. The reducing solution is recycled by pump 19 through line 18, fresh solution being introduced when necessary through line 21.
机译:1,162,328。从催化剂中回收氯化汞。 KNAPSACK A.G.,1968年4月2日[1967年4月4日],第15742/68号。标题C1A。 [也在C7区]通过用缺乏的O 2或空气燃烧C从受污染的惰性HgCl 2 /活性C催化剂中回收Hg以主要产生CO,该混合物由气态Hg,HgCl 2和H将Hg 2 Cl 2排出或升华(与燃烧气体一起),将混合物冷凝,并通过添加还原剂(例如硫酸肼,硫酸亚铁)将HgCl 2和Hg 2 Cl 2还原为Hg。或甲醛。如图所示,惰性催化剂9在竖炉3中燃烧。产物通过管线10离开炉并在管式冷凝器11中冷却。冷凝物和燃烧气体通过管线13到达洗涤塔14,洗涤塔14被供应还原溶液15。在17处将其排出,而在除去氯化汞污染物并还原后,燃烧气体通过管线16离开并燃烧。还原溶液由泵19通过管线18再循环,必要时通过管线21引入新鲜溶液。

著录项

  • 公开/公告号DE1558415A1

    专利类型

  • 公开/公告日1970-03-19

    原文格式PDF

  • 申请/专利权人 KNAPSACK AG;

    申请/专利号DE19671558415

  • 发明设计人 ARMIN JACOBOWSKYDIPL.-CHEM.DR.-ING.;

    申请日1967-04-04

  • 分类号C22B5/16;

  • 国家 DE

  • 入库时间 2022-08-23 11:09:23

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