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    • 1. 发明专利
    • Glass melting furnace-exhaust gas treatment method and treatment apparatus
    • 玻璃熔炼炉 - 排气处理方法和处理装置
    • JP2006075764A
    • 2006-03-23
    • JP2004263874
    • 2004-09-10
    • Babcock Hitachi Kkバブコック日立株式会社
    • NAGAI YOSHINORIKATSUBE TOSHIOINATSUNE YOSHIROUMORITA ISATO
    • B01D53/56B01D53/34B01D53/50B01D53/77
    • PROBLEM TO BE SOLVED: To provide a glass melting furnace-exhaust gas treatment method enabling the treatment of the exhaust gas generated from a glass melting furnace with a high reliability and a high efficiency, and its treatment apparatus. SOLUTION: (1) The glass melting furnace-exhaust gas treatment method comprises steps of adding an alkali neutralizer to the exhaust gas generated from the glass melting furnace to make the sulfur oxide in the exhaust gas to a sulfate compound, removing the produced product by a dust removing operation, thereafter, maintaining the exhaust gas temperature in the range of 200-300°C, and in supplying the exhaust gas into an exhaust gas denitrization equipment provided with a catalyst layer to remove nitrogen oxides in the exhaust gas under a reducer, injecting the reducer when the exhaust gas temperature at an outlet of the catalyst layer reaches not less than 130°C. (2) The exhaust gas treatment method comprises heating the catalyst layer of the exhaust gas denitrization equipment to not less than 100°C before the exhaust gas denitrization equipment is started up. COPYRIGHT: (C)2006,JPO&NCIPI
    • 解决的问题:提供一种能够以高可靠性和高效率处理从玻璃熔炉产生的废气的玻璃熔融炉废气处理方法及其处理装置。 (1)玻璃熔融炉废气处理方法包括以下步骤:向由玻璃熔炉产生的废气中加入碱中和剂,使废气中的硫氧化物形成硫酸盐化合物,除去 然后将废气温度维持在200-300℃的范围内,并将排气供给到具有催化剂层的排气脱硝装置中以除去排气中的氮氧化物 在减速机下方,当催化剂层出口处的排气温度达到130℃以上时,注入还原剂。 (2)废气处理方法包括在排气脱硝装置起动之前将废气脱硝装置的催化剂层加热至不低于100℃。 版权所有(C)2006,JPO&NCIPI
    • 3. 发明专利
    • AMMONIA INJECTION DEVICE
    • JPH10216475A
    • 1998-08-18
    • JP2370197
    • 1997-02-06
    • BABCOCK HITACHI KK
    • WADA TOSHIMICHIISHIKAWA TOMIHISAMURATAKA TATSUOINATSUNE YOSHIROUMORI YOSHIMICHI
    • B01D53/56B01D53/74
    • PROBLEM TO BE SOLVED: To accurately adjust and make operation of ammonia injection and scattering easy by arranging plural broad division distribution control valves each for an ammonia supply quantity per section in a waste duct which is divided in plural sections and connecting at least two injection pipes by which ammonia distribution control can be made per valve to the valves downstream thereof. SOLUTION: Broad division distribution valves 2 corresponding to broad divisions in a waste gas duct 6 are each provided with an orifice 3a of a flow meter, and at least two ammonia injection pipes 5 are installed per broad division distribution valve 2. Medium division distribution valve 4 is installed per ammonia injection pipe 5. First, the broad division distribution valves 2 are used to adjust NOx concentration distribution at an outlet of a denitrification device so that the average is equal per zone of the outlet zone. Since the number of the broad division distribution valves 2 is small, adjustment operation of injection scattering of ammonia is relatively easily done. Adjustment of NOx concentration varying in the broad divisions of the duct is made by the medium division distribution valves 4, and as a result, highly accurate and easy operation of injection scattering is done, and denitrificating efficiency and work efficiency are improved.
    • 7. 发明专利
    • AMMONIA INJECTION APPARATUS
    • JPS60132624A
    • 1985-07-15
    • JP24005583
    • 1983-12-20
    • BABCOCK HITACHI KK
    • MORI YOSHIMICHIINATSUNE YOSHIROU
    • B01D53/56F23J15/00
    • PURPOSE:To prevent the accumulation of dust and to stably maintain proper NH3- injection for a long period of time corresponding to the NOx- amount in a duct in vertical and horizontal directions, by extending the length of a nozzle in an NH3- injection apparatus for denitrating waste gas. CONSTITUTION:In an NH3- injection apparatus wherein an injection pipe 5 having several injection nozzles 6 arranged therein in parallel to a gas stream is arranged in a duct in order to inject NH3 into a waste gas denitrating apparatus as a reducing agent, the length of each nozzle arranged in the injection pipe 5 is extended forwardly from the stay part of gas to be treated generated by the injection pipe 5. If the length of the nozzle is set to one 2-3 times on the basis of the diameter (D) of the injection pipe, injected NH3 is carried on the gas stream to be uniformly flowed to a downstream catalyst layer and the solidification and growth of dust is prevented while each nozzle is prevented from clogging caused by the adhesion of dust to the injection part thereof.