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SIMULTANEOUS REMOVAL OF SO2 AND H2S FROM EXHAUST GASES
SIMULTANEOUS REMOVAL OF SO2 AND H2S FROM EXHAUST GASES
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机译:同时去除排气中的SO2和H2S
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摘要
Process for a simultaneous removal of SO2 and H2S from exhaust gases in which the exhaust gases are contacted in a first stage in a countercurrent operation with a first suspension, which contains 60 to 95 g/l ZnSO3, 80 to 90 g/l ZnO, and 0.1 to 1.0 g/l ZnS. 40 to 60% by volume of the suspension collected in the sump of the first stage are recycled and are re-supplied to the first stage at its top. The exhaust gas which has been depleted of SO2 and H2S is contacted in a second stage in a countercurrent operation with a second suspension, which contains 80 to 150 g/l ZnO, and with a third suspension, which contains 60 to 95 g/l ZnSO3, 80 to 90 g/l ZnO, and 0.1 to 1.0 g/l ZnS 40 to 60% by volume of the suspension which as been collected in the sump of the secnd stage are recycled and are re-supplied as the third suspension to the second stage at its top. The pure gas is withdrawn from the second stage at its top.
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机译:从废气中同时去除SO2和H2S的方法,其中废气在第一阶段中与第一悬浮液逆流接触,该第一悬浮液包含60至95 g / l ZnSO3、80至90 g / l ZnO,和0.1至1.0 g / l ZnS。回收在第一阶段集液槽中收集到的悬浮液的40%至60%(按体积计),并在第一阶段的顶部重新提供给第一阶段。耗尽了SO2和H2S的废气在第二阶段中以逆流方式与包含80至150 g / l ZnO的第二悬浮液和包含60至95 g / l的第三悬浮液接触将ZnSO3、80至90 g / l ZnO和0.1至1.0 g / l ZnS 40至60体积%的悬浮液回收,这些悬浮液在第二阶段的集液槽中收集,然后作为第三种悬浮液重新提供给第二阶段在其顶部。从第二阶段的顶部抽出纯净气体。
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