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CHLORINE BYPASS EXHAUST GAS TREATMENT METHOD AND CHLORINE BYPASS SYSTEM

机译:氯气除气处理方法及氯气除气系统

摘要

PROBLEM TO BE SOLVED: To stably treat a chlorine bypass exhaust gas while suppressing equipment cost to be low.SOLUTION: While a part G1 of a combustion gas is cooled, extraction is performed from a kiln exhaust gas flow passage from the tail of a cement kiln 2 to the lowermost cyclone, and chlorine bypass dust D5 is recovered from extraction gases G3, G4. The gas G5 after the recovery is added with a powdery desulfurizing agent DA, and before the gas G6 after the addition of the desulfurizing agent is joined to the exhaust gas system of a cement firing apparatus, dust is removed from the gas after the addition of the desulfurizing agent. It is possible that a part of the dust removal dust D6 is added to the gas after the recovery of chlorine bypass dust as a part of the desulfurizing agent, and is added to cement. It is possible that, after the recovery of the chlorine bypass dust, the concentration of SOin the gas before and after the addition of the desulfurizing agent is measured, and the addition amount of the desulfurizing agent can be controlled in accordance with both SOconcentrations.SELECTED DRAWING: Figure 1
机译:解决的问题:稳定地处理氯旁路废气,同时降低设备成本。解决方案:冷却一部分燃烧气体G1时,从水泥尾部从窑尾废气流道中抽气。窑2到最下部的旋风分离器,氯气旁路粉尘D5从提取气体G3,G4中回收。回收后的气体G5中添加了粉末状的脱硫剂DA,在添加了脱硫剂之后的气体G6与水泥烧成装置的排气系统接合之前,在添加了脱硫剂的气体之后除去了灰尘。脱硫剂。除尘粉尘D6的一部分可以在回收氯旁路粉尘后作为脱硫剂的一部分添加到气体中,并添加到水泥中。有可能在回收氯旁路粉尘之后,测量了在添加脱硫剂之前和之后的气体中的SO浓度,并且可以根据两种SO浓度来控制脱硫剂的添加量。图:图1

著录项

  • 公开/公告号JP2017031033A

    专利类型

  • 公开/公告日2017-02-09

    原文格式PDF

  • 申请/专利权人 TAIHEIYO CEMENT CORP;

    申请/专利号JP20150155852

  • 发明设计人 TERASAKI JUNICHI;UENO NAOKI;

    申请日2015-08-06

  • 分类号C04B7/60;B01D53/83;B01D53/50;F27D17;

  • 国家 JP

  • 入库时间 2022-08-21 13:59:28

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