首页> 外国专利> METHOD FOR DIRECTLY PREPARING A SULPHATE OR SULPHATES FROM EXHAUST GASES CONTAINING SO2 GAS

METHOD FOR DIRECTLY PREPARING A SULPHATE OR SULPHATES FROM EXHAUST GASES CONTAINING SO2 GAS

机译:从含SO2气体的排气中直接制备硫酸盐或硫酸盐的方法

摘要

1409593 Sulphur dioxide from gases OSAKA KOHAI CO Ltd 16 March 1973 [18 March 1972] 12734/73 Heading C1A SO 2 is removed from O 2 -containing waste gases and Ca or Mg sulphate prepared by contacting the gases in an alkaline region with an aqueous liquor containing a Ca- and/or Mg-containing compound and a Mn (II) salt in an amount sufficient to form MnO 2 with dissolved O 2 thereby forming a sulphite, contacting the resultant liquor in an acidic region with further waste gases to oxidize the sulphite to sulphate with the aid of O 2 in the waste gases. The Ca or Mg compound may be CaCO 3 , Ca(OH) 2 , Mg(OH) 2 , MgCO 3 and/or dolomite. The Mn (II) salt may be MnCl 2 or MnSO 4 in an amount of at least 0À00077 mol/l. Waste gases containing O 2 and 0À15% by vol. SO 2 may be scrubbed countercurrently by a slurry of Ca(OH) 2 and MnCl 2 sprayed via 10 into the alkaline region of tower 3. The CaSO 3 -containing liquor formed passes into the acidic tank 2 where the liquor is mixed with the incoming SO 2 and O 2 -containing waste gas which oxidizes the sulphite into sulphate. The acidic liquor is then passed to separator 6 to remove the solid CaSO 4 , the mother liquor then being recycled via make-up tank 7 to spray heads 10. MgSO 4 may be removed from the acidic liquor by neutralizing with Mg(OH) 2 , scrubbing with SO 2 gases and then cooling the resulting liquor.
机译:1409593气体中的二氧化硫大阪KOHAI CO有限公司1973年3月16日[1972年3月18日] 12734/73标题C1A SO 2从含O 2的废气和通过使碱性区域中的气体与水接触的硫酸钙或硫酸镁去除含有含Ca和/或Mg的化合物和Mn(II)盐的量足以与溶解的O 2形成MnO 2从而形成亚硫酸盐的液体,使所得液体在酸性区域与其他废气接触以氧化借助废气中的O 2将亚硫酸盐转化为硫酸盐。 Ca或Mg化合物可以是CaCO 3,Ca(OH)2,Mg(OH)2,MgCO 3和/或白云石。 Mn(II)盐可以是MnCl 2或MnSO 4,其含量至少为0-00077 mol / l。含有O 2和0-15%(体积)的废气SO 2可以通过Ca(OH)2和MnCl 2的浆液逆流洗涤,该浆液通过10喷入塔3的碱性区域中。所形成的含CaSO 3的液体进入酸性罐2,在此处将液体与进料混合含SO 2和O 2的废气,将亚硫酸盐氧化成硫酸盐。然后将酸性液体传递至分离器6以去除固体CaSO 4,然后将母液通过补充罐7再循环至喷头10。可以通过用Mg(OH)2中和从酸性液体中去除MgSO 4。 ,用SO 2气体洗涤,然后冷却所得液体。

著录项

  • 公开/公告号GB1409593A

    专利类型

  • 公开/公告日1975-10-08

    原文格式PDF

  • 申请/专利权人 OSAKA KOHAI CO LTD;

    申请/专利号GB19730012734

  • 发明设计人

    申请日1973-03-16

  • 分类号B01D53/34;C01F5/40;C01F11/46;

  • 国家 GB

  • 入库时间 2022-08-23 03:37:07

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