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    • 74. 发明申请
    • PROCESS FOR SEPARATING SO2 and NOx
    • 分离SO2和NOx的方法
    • WO1986000243A1
    • 1986-01-16
    • PCT/EP1985000295
    • 1985-06-19
    • BERGWERKSVERBAND GMBHJÜNTGEN, HaraldPETERS, WernerKNOBLAUCH, KarlRICHTER, EkkehardGROCHOWSKI, Horst
    • BERGWERKSVERBAND GMBH
    • B01D53/36
    • B01D53/8637B01D53/60Y02A50/2344
    • A process for separating SO2 and NOx, especially from combustion gases, in which the first stage is to separate the majority of the SO2 and a small proportion of the NOx from the combustion gas, and the second stage is to separate the majority of the NOx from the combustion gas by catalysis using activated carbon or activated coke with the addition of ammonia, and to separate the residual SO2 by reaction with the ammonia. The active carbon/active coke is fed into a reactor, and the loaded adsorption agent is removed from the reactor and regenerated thermally or by washing. The adsorption agent can also be passed through a sieve and again fed into the reactor, after separation of the ammonium sulphate, for the purpose of reuse. Ammonia can be recovered from the washing water of the active carbon/active coke washing operation as well as from the ammonium sulphate which has been passed through the sieve, after which it can be returned to the separation process.
    • 一种用于分离特别是燃烧气体的SO 2和NO x的方法,其中第一阶段是从燃烧气体中分离大部分SO 2和一小部分的NOx,第二阶段是分离大部分的NOx 从燃烧气体中通过使用活性炭或活性焦炭通过催化加入氨,并通过与氨的反应来分离残余的SO 2。 将活性炭/活性焦炭进料到反应器中,并将负载的吸附剂从反应器中取出并热再生或通过洗涤。 为了再利用,吸附剂也可以通过筛子并再次进料到反应器中,在分离硫酸铵之后。 可以从活性炭/活性焦炭洗涤操作的洗涤水以及已经通过筛子的硫酸铵中回收氨,然后可以将其返回到分离过程。