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    • 1. 发明专利
    • FLUIDIZED BED COMBUSTION METHOD
    • JPS6341708A
    • 1988-02-23
    • JP18598786
    • 1986-08-07
    • KAWASAKI HEAVY IND LTD
    • HORI KIKUOKIKUZAWA KIYOSHIOKADA ZENSHI
    • F23C10/00F23C10/28
    • PURPOSE:To obtain a highly stable combustion efficiency and a stable high- temperature waste gas by setting the temperature of a free board outlet gas higher than the temperature of the fluidized bed and controlling the temperature by changing the ratio of primary air to secondary air. CONSTITUTION:A fluidized bed 4 is provided on the upper side of a wind box 2 through an air dispering plate 3 and a free board 5 is provided on the upper side of the fluidized bed 4. A heat transfer tube 6 is provided within the fluidized bed 4. Coal is changed into the fluidized bed 4 through a coal supply port 7 and are burnt. A primary air supply tube 8 is connected to the wind box 2 and a flow meter 10 and a fl-adjusting valve 11 are provided in the tube 8. Further, a secondary air supply tube 12 is connected to the free board 5, and a flow meter 13 and a flow adjusting valve 14 are provided in the tube 12. The amount of air passing through the heat transfer tube 6 is determined so that the fluidized-bed temperature is in the range 800-900 deg.C, and the ratio of primary air to secondary air is changed to control the free board outlet temperature so that it becomes a predetermined temperature of 1000-1400 deg.C.
    • 2. 发明专利
    • CONTROLLING METHOD AND DEVICE FOR MIXED-PRESSURE BACK-PRESSURE EXTRACTION STEAM TURBINE PLANT
    • JPS62142810A
    • 1987-06-26
    • JP28244185
    • 1985-12-16
    • KAWASAKI HEAVY IND LTD
    • HORI KIKUOHORIIE HIROSHI
    • F01K7/20F01K7/38
    • PURPOSE:To aim at simplification of the structure and control system of a turbine by controlling the back-pressure, medium-pressure extraction steam pressure and pressures of the mixed-pressure system in a mixed-pressure back-pressure extraction steam turbine by means of control valves in response to pressures at the fixed places respectively. CONSTITUTION:The captioned plant is provided with a coal-fired boiler 3 as a high- pressure boiler, a recovery boiler 1 as a medium-pressure boiler, an extraction steam turbine 2 and a mixed-pressure back-pressure extraction steam turbine 14. In addition, the steam line 20 from a coal-fired boiler 3 is connected to the entrance of the turbine 14, and the steam line from the recovery boiler 1 is connected to the turbines 2, 14 respectively. Hereupon, to the back steam line 7 of the turbine 14 is connected an exhaust cooler 15, and the back-pressure is controlled by means of a control valve 16 provided at the entrance of the exhaust cooler 15 in response to pressures in the line 7. In addition, the medium-pressure extraction steam pressure and pressures of the mixed-pressure system are controlled by means of control valves 13, 8, provided on a medium-pressure extraction steam line 12 and the steam line 20 respectively, in response to the pressure in the steam lines 12, 10 respectively.
    • 6. 发明专利
    • DRY MOVING LAYER REACTION METHOD FOR EXHAUST GAS FROM INCINERATOR AND ITS DEVICE
    • JPS5594620A
    • 1980-07-18
    • JP315779
    • 1979-01-12
    • KAWASAKI HEAVY IND LTD
    • MORIOKA SHIYUUICHIHORI KIKUOTAKASU NOBUAKIIDE YOSHIHIRO
    • B01D53/68B01D53/08B01D53/14B01D53/18
    • PURPOSE:To improve the utilization rate of quicklime by a method wherein exhaust gas from an incinerator is passed through an upper portion of a moving reaction layer, into which quicklime grains are filled, so that the exhaust gas flow crosses at right angles with the movig reaction layer, and exhaust gas is passed through the lower portion in the direction opposite to the exhaust gas. CONSTITUTION:The both sides of a moving reaction layer 1, of which CaO grains are filled among support bodies 3 in stratiform and movement-possible shapes, are partitioned into an upper portion and a lower portion from a portion near a central portion, exhaust gas from an incinerator is passed through the upper portion 5 so that the exhaust gas cross at right angles with the reaction layer, and the exhaust gas from the incinerator is passed through the lower portion 6 in the direction opposite to an exhaust gas flow of the upper portion 5. When the exhaust gas is introduced from one side of the upper portion 5, the gas contacts with the CaO grains falling at low speed to produce CaCl2 and CaSO4. When the CaO grains reach the lower portion 6, the grains contact with the exhaust gas induced in the opposite direction, and CaO not reacted yet reacts with the gas. Thus, the segregation of minute particles is eliminated by an exhaust gas flow in the opposite direction, and the increase of pressure loss is prevented.