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    • 12. 发明专利
    • COMBINED POWER PLANT UTILIZING GASIFIED COAL
    • JPS6069221A
    • 1985-04-19
    • JP17711583
    • 1983-09-27
    • HITACHI LTDHITACHI ENG CO LTD
    • NAGASAKI NOBUONOGUCHI YOSHIKI
    • F01K23/02C10J3/02C10J3/20F01K13/00F01K23/06F01K23/10F02C3/22F02C6/10
    • PURPOSE:To raise the thermal efficiency of a power plant, by heating air or oxygen gas serving as a gasifier by the gas produced by a gasifying furnace and dedusted by a precision dedusting means which is disposed at the outlet of a steam generating means at the outlet of the gasifying furnace. CONSTITUTION:A steam generating means 7 disposed at the outlet of a coal gasifying furnace 3 cools crude coal gas produced at the furnace 3 and carries steam generated at the steam generating means 7 to a waste-heat recovering boiler 20. The, the crude gas is carried to a precision dedusting means 63, in which dust contained in the crude gas is removed perfectly. A heat exchanger 64 is provided on the downstream side of the dedusting means 63 so as to preheat a gasifying agent such as air supplied to the coal gasifying furnace 3 by the dedusted crude coal gas. Further, a gasifying-agent passage 83 is provided to connect the heat exchanger 64 to a gas turbine 17 of a combined power plant 61 so that preheated gasifying agent is supplied to the coal gasifying furnace 3. With such an arrangement, it is enabled to raise the thermal efficiency of the power plant to a great extent, to lower the plant cost considerably and to improve operation of the power plant.
    • 14. 发明专利
    • COMBINED POWER PLANT
    • JPH03115707A
    • 1991-05-16
    • JP25299389
    • 1989-09-28
    • HITACHI LTDHITACHI ENG CO LTD
    • YANAI EIJIHATTORI YOICHINAGASAKI NOBUONOGUCHI YOSHIKIHOSHINO KAZUSADA
    • F01K23/10
    • PURPOSE:To improve the power generation efficiency by diverting existing steam turbine power generation equipment and existing water circulating system for condenser, adding gas turbine equipment and exhaust heat recovering boilers, and by carrying out effective hat recovery in the exhaust heat recovering boilers. CONSTITUTION:In steam turbine equipment, a high pressure turbine 21, an intermediate pressure turbine 22, a low pressure turbine 23, a condenser 25 and a generator 26 are left as a remaining part, and a feed water heater and a steam turbine extraction system to it are removed. Two units of gas turbine power generation equipment and two exhaust heat recovering boilers are added, and exhaust gas 6 used at a gas turbine 3 is sent to an exhaust heat recovering boiler 10 so as to heat hot water 14 supplied from the steam turbine equipment to generate steam. Condensed water at the condenser 25 is used for the hot water 14 and sent through a condensate pump 27. The steam generated by the boiler 10 is diverted to main steam 15 at high temperature and high pressure and reheated steam 16 at high temperature and intermediate pressure, and the main steam 15 is supplied to the high pressure turbine 21 and the reheated steam 16 to the intermediate turbine 22 respectively.
    • 15. 发明专利
    • COMPOSITE POWER GENERATION PLANT
    • JPH0350302A
    • 1991-03-04
    • JP18262489
    • 1989-07-17
    • HITACHI LTDHITACHI ENG CO LTD
    • HATTORI YOICHINAGASAKI NOBUOYANAI EIJINOGUCHI YOSHIKI
    • F01K23/10
    • PURPOSE:To improve the heat efficiency of a plant by constructing one cycle with plural exhaust heat recovery boilers, and installing a superheater which heats the steam supplied to a steam turbine at the uppest-stream part of the exhaust heat recovery boiler which the hottest exhaust heat enters. CONSTITUTION:For a composite power generation plant consisting of two gas turbines 1, 2 of different types, two exhaust heat recovery boilers 3, 4 of different bank structures corresponding to respective gas turbines 1, 2 and one steam turbine 5, one cycle is constructed with both the exhaust heat recovery boilers 3, 4. Namely, water supply is carried out for the respective exhaust heat recovery boilers 3, 4 by a feed water pump 14, and is heat-exchanged with exhaust gas by economizers 16 in respective boilers 3, 4 for high temperature water. After it joins the flow of the high temperature water which gets out of the respective economizers 16, it is fed to the evaporator 17 of the exhaust heat recovery boiler 4 and is heated for saturated steam. The saturated steam is fed to the superheater 18 of the exhaust heat recovery boiler 3, and the heated steam is fed to a steam turbine 5.
    • 18. 发明专利
    • Coal supplying method and apparatus for coal gasification electric power plant
    • 煤炭燃气发电厂煤炭供应方法及装置
    • JPS61114009A
    • 1986-05-31
    • JP23500384
    • 1984-11-09
    • Hitachi Eng Co LtdHitachi Ltd
    • NAGASAKI NOBUONOGUCHI YOSHIKI
    • F01K23/02C10J3/46F01K23/10F23K3/00F23K3/02
    • Y02E20/18
    • PURPOSE: To prevent a back-fire from a gasification furnace, a coal dust exprosion at a coal supplying system and improve safety by a method wherein pulverized coal is supplied to a gasification furnace by utilizing of inactive gas produced and seperated from the system of a composite electric plant at coal gasification.
      CONSTITUTION: Cabon deoxide remaining in purification gas 28 is contacted with absorbing liquid at a decarbonate tower 75 and is absorbed only in a amount necessary for the coal supply. The absorbing liquid absorbed the carbon deoxide is sent to a reclaim tower 77 and the absorbed carbon deoxide is seperated by reducing pressure and heating, thereafter, it is reclaimed and used in a circulation. The carbon deoxide is seperated from the reclaim tower 77 in this process. The inactive gas 80, having the carbon deoxide as principal component which is obtained by above mentioned process, is pressurized by a pressurizing compressor 81 to be supplied to a lock hopper 3. According to this method, the back-fire and or the coal dust exprosion are prevented and the safety may be improved.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:为了防止气化炉的反火,煤供应系统中的煤尘暴露,并且通过利用从系统中产生和分离的不活泼气体将气化炉供应给气化炉的方法来提高安全性 煤气化复合电厂。 构成:保留在净化气体28中的脱氧化钯与在碳酸氢盐塔75处的吸收液接触,并且仅以煤供应所需的量吸收。 吸收碳酸氢盐的吸收液被送到回收塔77,通过减压和加热分离吸收的碳酸氢盐,然后回收再循环使用。 在该过程中,碳酸氢盐与回收塔77分离。 以上述方法获得的具有作为主要成分的碳氧化物的惰性气体80由加压压缩机81加压,供给到封闭料斗3.根据该方法,背火和/或煤尘 防止了侵蚀,可以提高安全性。