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    • 15. 发明专利
    • FUEL FEEDING METHOD
    • JPS63169412A
    • 1988-07-13
    • JP31074286
    • 1986-12-27
    • MITSUBISHI HEAVY IND LTD
    • HASEGAWA KOJIARAKAWA YOSHIHISAMIYAMOTO MANABU
    • F23C10/18F23C10/22
    • PURPOSE:To vaporize a moisture content on the surface of solid fuel by means of a sensible heat by particles, by a method wherein high temperature particles collected from combustion exhaust gas exhausted from a fluidized bed combustion furnace are mixed with solid fuel, and thereafter, gas is carried and is fed in a fluidized bed in the combustion furnace. CONSTITUTION:Solid fuel 3 is charged in a fuel hopper 5 through a fuel feed pipe 4, and is introduced through a takeout valve 6 to a fuel-particle mixer 7. To the mixer, particles, collected from combustion exhaust gas exhausted from a combustion furnace 1 and having temperature of about 100-400 deg.C, are introduced through a particle recirculating pipe 8, and are mixed with the solid fuel 3. The mixing causes vaporization of a part or all of a moisture content on the surface of the solid fuel 3 by means of a sensible heat possessed by the solid fuel. This method eliminates drying of the solid fuel as pretreatment. Since a moisture content on the surface of the solid fuel is vaporized in a mixer 7, choking is prevented from occurring in fuel feed systems 11-14.
    • 20. 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.