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    • 13. 发明专利
    • FLUIDIZED LAYER HEAT EXCHANGER
    • JP2000257807A
    • 2000-09-22
    • JP5870999
    • 1999-03-05
    • MITSUBISHI HEAVY IND LTD
    • ARAKAWA YOSHIHISAKUROISHI TOSHIROMIYAMOTO MANABU
    • F23C10/02F22B1/02
    • PROBLEM TO BE SOLVED: To provide a fluidized layer heat exchanger reducing the corrosion of a relatively high-temperature heat exchanger such as a super-heater or the like in a circulating fluidized bed boiler. SOLUTION: In a fluidized layer heat exchanger 140, separating particles from two-phase stream containing combustion gas and the particles produced in the furnace 110 of a circulating fluidized bed boiler 110 and recovering heat from at least one part of the separated particles, then, supplying the particles into the furnace 100 again after recovering heat, an upstream side first chamber and a downstream side second chamber are provided in the fluidized layer heat exchanger 140 in reference to the moving direction in the fluidized layer heat exchanger 140 of the particles running from the fluidized layer heat exchanger 140 toward the furnace 110 while a first heat exchanger 144, through which relatively low temperature operating fluid flows, is arranged in the first chamber and a second heat exchanger 146, through which relatively high temperature operating fluid flows, is arranged in the second chamber.
    • 15. 发明专利
    • Remover for hydrogen chloride and sulfer dioxide
    • 去除氯化氢和二氧化硫
    • JPH11276851A
    • 1999-10-12
    • JP8064898
    • 1998-03-27
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • MIYAMOTO HITOSHIKOJIMA KATSUHISAMIYAMOTO MANABUTAKIMOTO SHINICHI
    • B01D53/68B01D53/34B01D53/50B01D53/81
    • PROBLEM TO BE SOLVED: To prevent and check corrosion of a heating tube or the like while removal efficiency of hydrogen chloride and/or sulfer dioxide is improved by a method wherein a granular desalting and a desulfurizing agents are filled in a container equipped with a gas flow passage up and down, and an exhaust gas temperature is kept within a specific range.
      SOLUTION: An apparatus which generates hydrogen chloride and sulfur dioxide, for example, a dry distillating furnace or a combustion furnace 8 is generally operated at near 500°C, and a gas 6 containing hydrogen chloride gas and sulfur dioxide gas in addition to hydrogen, nitrogen, carbon monoxide, or the like is generated by the operation. The gas 6 is conducted to a desalting and desulfurizing tower 1. For the desalting and desulfurizing tower 1, a desalting and a desulfurizing agents 2 are filled inside, and the gas 6 is ventilated from a lower part of the tower 1. As the desalting and desulfurizing agent 2, CaO, Ca(OH)
      2 , or the like are used. After reaction-treating the gas 6 in the desalting and desulfurizing tower 1 in the state wherein an exhaust gas temperature is kept within a range of 350 to 550°C, the gas 6 as a treating gas 5 is sent to an exhaust gas boiler 9 and burnt.
      COPYRIGHT: (C)1999,JPO
    • 要解决的问题:为了防止和检查加热管等的腐蚀,同时通过将颗粒状脱盐和脱硫剂填充在装有气体的容器中的方法来提高氯化氢和/或二氧化硫的去除效率 上下流通,废气温度保持在特定范围内。 解决方案:产生氯化氢和二氧化硫的装置,例如干蒸馏炉或燃烧炉8通常在500℃附近运行,除了氢气之外还包含含有氯化氢气体和二氧化硫气体的气体6 ,通过该操作产生氮气,一氧化碳等。 气体6被导入脱盐脱硫塔1.对于脱盐脱硫塔1,将脱盐和脱硫剂2填充到内部,气体6从塔1的下部通风。作为脱盐 和脱硫剂2,CaO,Ca(OH)2等。 在排气温度保持在350〜550℃的范围内的条件下,对脱盐脱硫塔1中的气体6进行反应处理后,将作为处理气体5的气体6送入废气锅炉 9并烧了
    • 17. 发明专利
    • COMBUSTION METHOD FOR FLUIDIZED BED
    • JPS6329104A
    • 1988-02-06
    • JP17119686
    • 1986-07-21
    • MITSUBISHI HEAVY IND LTD
    • HONDA KEISUKEARAKAWA YOSHIHISAMIYAMOTO MANABU
    • F23C9/06F23C9/08F23C10/00F23C10/02
    • PURPOSE:To improve combustion efficiency and reduce the generation of NOx markedly by a method wherein the controlled amount of air is supplied into a fluidized bed and remaining air is supplied to the upper part of the fluidized bed and a part of low temp. particles caught from the exhaust gas flowing out of the bed is recirculated into the bed. CONSTITUTION:Fuel charged from a fuel feeder 6 and solids including unburnt carbon charged from charging nozzles 41, 42 for solids make reaction with a primary air of which quantity is 0.3-0.8 times the theoretical air quantity in a fluidized bed 5 and fuel is gasified and a part of the fuel is burnt to form a primary burning range of reducing atmosphere. Reductive gas etc. generated in the primary combustion range are introduced into the range for unburnt part at the upper part of the bed 5 and overfire air is charged from a nozzle 7 and a denitration reaction is performed. After that, unburnt part of fuel and remaining reducing gas flow into a perfect combustion range to promote perfect burning. The solids caught by a cyclone separator 16 and an electric precipitator 21 of which quantity is 1-5 times the amount of fuel are charged into the bed 5 through the nozzles 41, 42 and the remainder is discharged outside a system.
    • 20. 发明专利
    • COMBUSTION DEVICE
    • JPH11201423A
    • 1999-07-30
    • JP323998
    • 1998-01-09
    • MITSUBISHI HEAVY IND LTD
    • SAITO KEISHIROBANDAI SHIGEMIMIYAMOTO MANABU
    • F23G5/027F23G5/30
    • PROBLEM TO BE SOLVED: To improve a heat efficiency by suppressing useless heat dissipation toward outside in a combustion device where the fluidized-bed-type dry distillation oven of a solid fuel and the combustion oven of char being generated by dry distillation in parallel and communicating with each other. SOLUTION: A combustion device is constituted by arranging a dry distillation oven 1 for performing the dry distillation of a solid fuel A by a high- temperature bubbling flow layer and a char combustion oven for burning the char content of a dry distillation residue in parallel and performing connection by seal pots 6 and 6' where the splash particles of a fluid material bubbling are deposited and fluid material circulation ports 7 and 7' at one edge and the other edge of each oven. The closed loop of a fluid material 3 is formed through the dry distillation oven 1 and the char combustion oven, thus preventing heat being accumulated at the fluid material 3 from being dissipated outside, reducing heat loss, and improving heat efficiency.