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    • 1. 发明专利
    • Exhaust gas dust removing apparatus and its operation method
    • 排气除尘装置及其操作方法
    • JP2005152746A
    • 2005-06-16
    • JP2003393423
    • 2003-11-25
    • Babcock Hitachi Kkバブコック日立株式会社
    • MORII SEIJIKAMEI NOBUHIROWATANABE KO
    • B01D46/42
    • PROBLEM TO BE SOLVED: To provide a continuously operable exhaust gas dust removing apparatus for collecting lumpy dust in an exhaust gas, and its operation method.
      SOLUTION: In this exhaust gas dust removing apparatus, partition plates 5 are provided so as to divide an almost horizontal duct and the almost vertical duct continued to the almost horizontal duct into a plurality of ducts along a gas flow direction, dampers 2 are provided to the almost horizontal duct parts in the respective ducts 6-9 partitioned by the partition plates 5, a dust sieve means 1 is provided to the almost vertical duct parts, the dampers 2 are controlled so as to be closed when the difference pressure in the exhaust gas flow channel between the upstream and downstream sides of the dust sieve means 1 becomes a set value or above but closed when the differential pressure is below the set value and dust recovering hoppers 3 are provided to the lower end parts of the almost vertical duct parts.
      COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:提供一种用于收集废气中的块状灰尘的可连续操作的废气除尘装置及其操作方法。 解决方案:在这种排气除尘装置中,分隔板5设置成将几乎水平的管道和几乎垂直的管道沿大致水平的管道分成沿气体流动方向的多个管道,阻尼器2 设置在由分隔板5分隔的各个管道6-9中的几乎水平的管道部分上,在几乎垂直的管道部分上设置有灰尘筛装置1,当阻尼器2的差压 在尘埃筛装置1的上游侧和下游侧之间的排气流动通道变为设定值以上,但当压差低于设定值时关闭,并且将灰尘回收料斗3设置在几乎 垂直管道部件。 版权所有(C)2005,JPO&NCIPI
    • 5. 发明专利
    • APPARATUS FOR DENITRATION TREATMENT
    • JPH01310723A
    • 1989-12-14
    • JP13993488
    • 1988-06-07
    • BABCOCK HITACHI KK
    • WATANABE KOISHIKAWA TOMIHISAMUKAI MASATO
    • B01D53/94
    • PURPOSE:To prevent lowering of heat efficiency by arranging a dust collector upstream of a waste heat recovery equipment, which is installed downstream of a denitration equipment, and another dust collector downstream of the waste heat recovery equipment and by returning the ash collected by both dust collectors to a flue gas generating equipment through an ash recycle line. CONSTITUTION:A flue gas produced by a boiler 1 has most of its dust collected by a dust collector 31 after denitrated by a denitration equipment 2, has its sensitive heat recovered by an air heater 3, has the rest of dust further collected perfectly by another dust collector 4 installed downstream of the air heater 3 and is ejected out of a stack 6 after passing through a desulfurization equipment 5. The dust collected by the dust collectors 31 and 4 is sent to the boiler 1 through a dust recycle line 13 and burnt again to increase heat efficiency. Catalyst poisoning is also lowered by collecting the ash at a high temperature to decrease heavy metal components contained in the ash.
    • 6. 发明专利
    • CONTROL DEVICE FOR AMOUNT OF AMMONIA TO BE INJECTED
    • JPS6219229A
    • 1987-01-28
    • JP15510185
    • 1985-07-16
    • BABCOCK HITACHI KK
    • WATANABE KO
    • B01D53/56B01D53/74B01D53/86F01N3/20G05D11/13
    • PURPOSE:To correspond in a period of the quick change of load by adding a molar ratio signal and a deviation signal of leak of NH3 from a detection signal of gas temp., a detection signal of NOX in an inlet, a detection signal of the flow rate of gas and a set signal of leak of NH3 and calculating a correcting signal of molar ratio. CONSTITUTION:A molar ratio signal 31 is calculated by inputting a detection signal 23 of gas temp., a detection signal 25 of NOX in an inlet, a detection signal 27 of the flow rate of gas and a set signal 29 of leak of NH3 outputted from an (S-NH3) setter 28 of leak of NH3 to an arithmetic device 30 of molar ratio. On the other hand, the detection signal 25, the molar ratio signal 31 and a detection signal 33 of NOX in an outlet are inputted to a computing element 34 of leak of NH3 and a calculation signal 35 of leak of NH3 is calculated and compared with the set signal 29. Then a deviation signal 37 of leak of NH3 is inputted to an adder 38 and added with the signal 31 and inputted to a multiplier 42 as a correcting signal 41 of molar ratio to calculate a signal 43 of the flow rate of the necessary NH3.
    • 8. 发明专利
    • METHOD AND APPARATUS FOR DENITRATING EXHAUST GAS
    • JPH11221446A
    • 1999-08-17
    • JP2553398
    • 1998-02-06
    • BABCOCK HITACHI KK
    • INATSUNE YOSHIROUWATANABE KO
    • B01D53/94
    • PROBLEM TO BE SOLVED: To provide an apparatus for denitrating exhaust gas having good denitration performance even under the conditions in which severe NOx regulation is required during the actuation of a waste heat recovering boiler, and a method for operating the apparatus. SOLUTION: The time for starting the injection of ammonia during the actuation of a denitration apparatus is set up at a point of time when the temperature of a denitration catalyst layer part reaches the boiling point or the vicinity of the boiling point of the condensed water of exhaust gas. Since the reduction of NOx can be attempted even in a low temperature area without lowering the activity of the denitration catalyst, the discharge of NOx can be controlled during the operation of a plant. Although an exhaust gas temperature at the outlet of the catalyst layer increases behind that at the inlet of the catalyst layer, when the injection of ammonia is started at 140 deg.C of an exhaust gas temperature at the inlet, an exhaust gas temperature at the outlet corresponds to 100 deg.C (the boiling point of the condensed water of exhaust gas), and since the temperature of the entire catalyst layer is at the lowest 100 deg.C when the injection of ammonia is started at this point of time, the discharge of ammonia or NOx into the air can be prevented.
    • 9. 发明专利
    • AMMONIA INJECTION DEVICE
    • JPH09173786A
    • 1997-07-08
    • JP33761595
    • 1995-12-26
    • BABCOCK HITACHI KK
    • HORIUCHI TERUHIROMORI YOSHIMICHIWATANABE KOMUKAI MASATO
    • B01D53/56B01D53/86B01D53/94
    • PROBLEM TO BE SOLVED: To solve the problem of unbalanced ammonia injection due to the reduction in injection amount of ammonia when the denitrification load lowers by mixing steam into the aqueous ammonia vapor to compensate the decrement of the aqueous ammonia vapor flow rate and apply the same pressure drop across one of nozzles as that before the decrease in aqueous ammonia vapor flow rate is caused, to each of the nozzles when the injection amount of aqueous ammonia vapor is reduced. SOLUTION: In this device, an aqueous ammonia vapor pipeline 10 is provided with a steam injection means downstream from a flow control valve 9 and steam is introduced to a steam pressure reducing valve 15 through a steam pipeline 14 to reduce the stream pressure to a value higher than the total value ((1)+(2)+(3)) of (1) the pressure drop across one of nozzles 13 at the time of allowing the aqueous ammonia vapor to flow at an intended flow rate, namely, at a flow rate before the reduction in injection amount of the aqueous ammonia vapor is caused, (2) the pressure drop across the aqueous ammonia vapor pipeline 10 and one of nozzle headers 11 and (3) the static pressure of a duct 2. When the amount of Nox produced reduced because of a change in denitrification load and accordingly, the injection amount of the aqueous ammonia vapor is reduced, steam is mixed into the aqueous ammonia vapor to compensate the decrement of the aqueous ammonia vapor flow rate and to maintain the injection velocity of the ammonia vapor at an intended nozzles 13 and further, to uniformly inject the aqueous ammonia vapor into the each of the nozzles 13 and further, to uniformly inject the aqueous ammonia vapor into the duct 2.
    • 10. 发明专利
    • DENITRATION EQUIPMENT
    • JPS62191026A
    • 1987-08-21
    • JP2989586
    • 1986-02-15
    • BABCOCK HITACHI KK
    • WATANABE KOARAKAWA HARUO
    • B01D53/94B01D53/86
    • PURPOSE:To allow the titled apparatus to withstand vibration, by arranging a box-shaped support member, which is formed of frame members surrounding the outer peripheries of a catalyst block aggregates and beam members connecting said frame members, in an exhaust gas passage and forming said aggregates into an integral structure by the box-shaped support member. CONSTITUTION:A box-shaped support member 33, which is formed of frame members 31-31c surrounding the outer peripheries of catalyst blocks 26a, 26b and beam members 32a, 32b connecting said frame members, is arranged in an exhaust gas passage and supported in an integral structure in such a state that the outer peripheries of the catalyst blocks 26a, 26b are surrounded through stopper members 34. Therefore, the box-shaped support member 33 has the same temp. as the catalyst blocks 26a, 26b and can be supported so as to follow thermal expansion and contraction. As a result, the box-shaped support member can be supported so as to withstand vibration.