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    • 11. 发明专利
    • EQUIPMENT FOR REGULATING FLOW RATE OF POWDER-GRAINS
    • JPH09280543A
    • 1997-10-31
    • JP9407596
    • 1996-04-16
    • MITSUBISHI HEAVY IND LTD
    • YAMADA KAZUJIOGIWARA KOTA
    • F23K3/02
    • PROBLEM TO BE SOLVED: To prevent occurrence of deflection in a flow of powder-grains and to reduce the area of installation of equipment for regulating 4 flow rate of powder-grains by having a plurality of damper blades which are so provided as to surround a flow passage of the powder-grains and are opened and closed with the circular-arc faces directed toward the upstream side of the passage. SOLUTION: A damper for regulating a flow rate of pulverized coal is provided for each of a plurality of pulverized coal tubes 15 connected to one coal pulverizer 16 and it regulates the amount of supply of the pulverized coal and also prevents a deflected flow thereof. Rotating shafts 3 are provided for the pulverized coal tube 15 and they are equipped with circular-arc-shaped damper blades 2 for opening and closing a flow passage 4 of the pulverized coal which are so provided as to close uniformly from the upstream side toward the downstream side. These damper blades 2 are fitted to the rotating shafts 3 in two sets being opposed to each other outside the passage 4 so that they are directed toward the upstream side of a flow 1 of the pulverized coal and closed from the upstream side to the downstream side around the rotating shafts 3. A flow rate detector 13 is fitted to a burner 12 and, based on an output signal thereof, the opening of each damper 10 is regulated by a control device 14.
    • 12. 发明专利
    • FINE POWDER COAL SEPARATOR DEVICE
    • JPH09264525A
    • 1997-10-07
    • JP7386896
    • 1996-03-28
    • MITSUBISHI HEAVY IND LTD
    • KAWASHIMA HACHIROOKAMOTO AKIYASUFUJIMURA KOUTAROUSUZUKI TAKESHIYAMADA KAZUJIISODA TAKAHIROSHIRAHATA TAKEHIKO
    • F23C99/00F23D1/00F23K3/02F23C11/00
    • PROBLEM TO BE SOLVED: To form a uniform flow speed distribution by a method wherein an outer diameter of a rich or lean separator at an axial center part of a fine powder coal pipe is a frustoconical shape with its flowing-in side being smaller than a flowing-out side, an outer diameter at the flowing-out part as well as a flowing-in side diameter and a flowing-out side diameter of a cut slit passing through an axial center line are made to have a rate of a specified range with the inner diameter of the fine powder coal pipe. SOLUTION: Fine powder coal mixture gas 02 is fed to a rich or lean separator 13 together with primary air. In this case, a slant angle θ of the frustoconical shape of the separator 13 is 60 deg. to 90 deg., an inner diameter of the fine powder coal pipe 05 is defined as D, a diameter d1 of a front flow side of a hollow recess slit is set to (1/10.5) D to (1/20.5) D, a diameter d2 at the rear stream side is set to (1/5.5) D to (1/10.5) D and an outer diameter d3 of the rich or lean separator 13 is set to (1/1.55) D to (1/3.5) D, thereby mixture gas at an outer side having a high fine powder coal concentration and a low fine powder coal concentration at a central part is formed in the fine powder pipe 05. With such an arrangement as above, it is possible to eliminate staying of gas caused by eddy flow which may easily be generated at a wall surface of the rear-side flow of the rich-lean separator 13 and to make a uniform flow speed distribution.
    • 15. 发明专利
    • METHOD FOR CONTROLLING CIRCULATING FLUIDIZED BED COMBUSTOR
    • JPH0413002A
    • 1992-01-17
    • JP11577990
    • 1990-05-07
    • MITSUBISHI HEAVY IND LTD
    • YAMADA KAZUJIIKUBO KUNIHIRO
    • F23C10/28F23C10/02
    • PURPOSE:To reduce the changes of the pressure differential between the upper part and the lower part in a combustor which is due to the load on the combustor by a method wherein the amount of the particles discharged from the combustor is controlled according to said pressure differential in the combustor and the load on the combustor in such a way as to make the pressure differential larger, the lower the load on the combustor becomes. CONSTITUTION:To a control box 4 are inputted a signal 11 representing the load on the boiler, a signal representing the pressure differential in the combustor sensed by a combustor-pressure differential meter 2, and a signal from a function generator 5; the control box 4 controls a particle-discharging device 3. The control adjusts the amount of the particles in the combustor 1 according to the load on the boiler so as to bring the combustor-pressure differential to a prescribed value represented by a line C. Therefore the generation of NOx, SOx, and unburned components in the combustor can be reduced in amount, thanks to reduced changes of the combustor-pressure differential, and furthermore, with the combustor-pressure differential confined within a planned range, the safety of the combustor can be enhanced.
    • 19. 发明专利
    • PULVERIZED COAL BURNER
    • JPH10332110A
    • 1998-12-15
    • JP14206397
    • 1997-05-30
    • MITSUBISHI HEAVY IND LTD
    • OKAMOTO AKIYASUTOKUDA KIMIYOKANEKO SHOZOYAMADA KAZUJIOGURI MASAHARU
    • F23D1/00
    • PROBLEM TO BE SOLVED: To prevent the distribution of the concentration of pulverized coal, which is set in a pulverized coal nozzle tube, from becoming abnormal, even in the case where a pulverized coal nozzle is vertically inclined in a pulverized coal burner having the pulverized coal nozzle provided in a swingable manner, in the vicinity of a top end of the pulverized coal nozzle tube for leading a mixture of the pulverized coal with transfer air to a burner. SOLUTION: This burner has a pulverized coal nozzle 104 disposed in a swingable manner by a nozzle driving shaft 118 in the vicinity of a top end of a pulverized coal nozzle tube 106. A pulverized coal concentration adjusting body 120 is mounted in the pulverized coal nozzle 104. The pulverized coal concentration adjusting body 120 is provided at its center with a coal-air mixture passage 121 and, further, a contracted flow passage 122 is formed between an outer peripheral face of the coal-air mixture passage 121 and an inner peripheral face of the pulverized coal nozzle 104. Concentration distribution is given to a coal-air mixture to be supplied from the pulverized coal nozzle 104, so that the concentration of the pulverized coal on the surface side of the coal-air mixture is made high while the concentration of the pulverized coal on the inner side of it is made low.
    • 20. 发明专利
    • BURNER NOZZLE
    • JPH10185110A
    • 1998-07-14
    • JP34530296
    • 1996-12-25
    • MITSUBISHI HEAVY IND LTD
    • YAMADA KAZUJISUDO TAKAYUKI
    • F23C99/00F23C11/00
    • PROBLEM TO BE SOLVED: To prevent damage of a nozzle, to improve a thermal efficiency and to reduce NOx and unburnt components by forming a gas nozzle on an outermost periphery of the nozzle and introducing combustion air and recirculating gas from another system. SOLUTION: A gas duct 6 is connected to a gas nozzle having a double structure by surrounding an outermost periphery of a nozzle 2 from four sides. Recirculating gas is guided from a system other than that for combustion air via gas ducts 11, 12, and supplied from the gas nozzle into a furnace. The combustion air 9 fed from a center of the nozzle 2 into a wind box 1 by a fan is injected into the furnace, and the recirculating gas is injected from the gas nozzle from its outer periphery. Thus, the nozzle 2 is cooled to effectively prevent damage of the nozzle 2. And, since the combustion air is used only for the combustion, excess air is reduced to improve thermal efficiency. Accordingly, NOX and unburnt components can be reduced.