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    • 2. 发明专利
    • Method for treating mercury in tail gas, and treatment system for tail gas
    • 尾气处理汞的方法及尾气处理系统
    • JP2009208078A
    • 2009-09-17
    • JP2009143177
    • 2009-06-16
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • HONJO SHINTAROTAKASHINA TORUOCHI EIJI
    • B01D53/64B01D53/34B01D53/50B01D53/56B01D53/77B01D53/86B01D53/94
    • PROBLEM TO BE SOLVED: To provide a method for treating a tail gas that can remove mercury and enables efficient operation and continuous performance without having a bad effect on an apparatus in a system. SOLUTION: The method for treating mercury in a tail gas includes subjecting the tail gas containing a nitrogen oxide, a sulfur oxide and mercury to reduction denitration in the presence of a solid catalyst after the addition of a chlorination agent and then performing wet desulfurization with an alkaline lean liquid. A predicted value of an inlet mercury concentration before the reduction denitration is calculated based on the mercury concentration in the tail gas measured after the wet desulfurization. The feed rate of the chlorination agent to be added before the reduction denitration is controlled based on the amounts of change of the above predicted value and a standard inlet mercury concentration by the method for treating mercury in a tail gas and a treatment system for the tail gas is provided. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种处理能够去除汞并且能够有效操作和持续性能的尾气的方法,而不会对系统中的设备造成不良影响。 解决方案:用于处理尾气中的汞的方法包括在加入氯化剂之后,在固体催化剂存在下,将含有氮氧化物,硫氧化物和汞的尾气经还原脱硝,然后进行湿 用碱性贫液液脱硫。 根据湿式脱硫后测定的尾气中的汞浓度计算还原脱硝前的入口汞浓度的预测值。 基于通过尾气处理汞的方法和尾部处理系统的上述预测值和标准入口汞浓度的变化量来控制在还原脱硝之前加入的氯化剂的进料速率 提供气体。 版权所有(C)2009,JPO&INPIT
    • 8. 发明专利
    • FLUE GAS TREATMENT
    • JPH1094714A
    • 1998-04-14
    • JP27155896
    • 1996-09-20
    • MITSUBISHI HEAVY IND LTD
    • OKAZOE KIYOSHIOCHI EIJIISHIHARA MAKIKAZUTAKASHINA TORU
    • B01D53/34B01D53/14B01D53/50B01D53/58B01D53/77
    • PROBLEM TO BE SOLVED: To provide a flue gas treating method in which the concentration of ammonia in flue gas after treatment is kept low by using a small-sized gas- liquid contact device provided with both a concurrent flow absorber and a countercurrent flow absorber. SOLUTION: A gas-liquid contacting device is provided with an introducing side tank 21 into which a liquid absorbent is fed, a concurrent flow introducing side absorber 2 installed extended upward from the introducing side tank 21 and for subjecting untreated flue gas to gas-liquid contact with the liquid absorbent in the introducing side tank 21, a bring-out side tank 22 arranged adjacent to the introducing side tank 21 and into which a liquid absorbent is separately fed, and a countercurrent flow bring-out side absorber 3 installed extended upward from the bring-out side tank 22 and for introducing flue gas brought out from the introducing side absorber 2 to subject it to gas-liquid contact with the liquid absorbent in the bring-out side tank 22. By using the gas-liquid contracting device, fly mist is removed from flue gas before flowing into the bring-out side absorber 3 to return it to the introducing side tank 21, and also pH of the liquid absorbent of the other absorber is controlled to a low value (for example, 4.0-5.0) at which ammonia is hardly diffused into flue gas.