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    • 3. 发明申请
    • PROCESS AND ARRANGEMENT FOR OPERATING A DRYER FED BY HEATING STEAM
    • METHOD AND SYSTEM FOR操作加热蒸汽施加DRYER
    • WO1996026404A1
    • 1996-08-29
    • PCT/EP1996000683
    • 1996-02-19
    • VEAG VEREINIGTE ENERGIEWERKE AG
    • VEAG VEREINIGTE ENERGIEWERKE AGHÄUSLER, AndreaBAUER, FranzHÖHNE, Hartmut
    • F26B23/00
    • F26B23/001Y02P70/405
    • The invention pertains to a process and arrangement for operating a dryer fed by heating steam, in particular a coal dryer (4), in a power plant. The aim of the invention is to integrate the energy of the exhaust vapors into the power generating process with the greatest possible degree of efficiency. This is achieved by superheating the saturated steam (21) with hot steam (15) and feeding the resulting superheated steam (22) into the low-pressure section of the steam turbine or into another steam turbine. To accomplish this the invention provides that the saturated steam line (12) is connected to a steam-steam heat exchanger (2) in the superheated steam line (1) and the steam line (13) of the steam-steam heat exchanger (2) is connected to the low pressure section of the steam turbine or another steam turbine.
    • 本发明涉及一种方法和用于加载的加热蒸汽干燥机的操作的装置,特别是煤干燥器(4)中,在发电厂。 本发明的基本目的是实现在电厂过程排气蒸气的高能积分以最高可能的效率。 这是这样实现的饱和蒸汽(21)通过过热,从而冷却过热蒸汽(16)和被引导到蒸汽涡轮机的低压部分或另一蒸汽涡轮机的过热蒸汽(22)的热蒸汽(15)。 对于根据本发明的实现是在热蒸汽管中的饱和蒸气线(12)与一(1)嵌入的气相蒸汽换热器(2)和蒸汽 - 蒸气换热器(2)的与所述蒸汽涡轮机的低压部分或另一蒸汽涡轮机的蒸汽管线(13) 连接。
    • 5. 发明授权
    • VERFAHREN ZUM BETREIBEN EINES KOMBIKRAFTWERKES
    • 一种用于操作联合循环电站
    • EP0651854B1
    • 1996-03-20
    • EP93914662.7
    • 1993-06-16
    • VEAG Vereinigte Energiewerke AG
    • BAUER, FranzWETZEL, Horst
    • F01K23/06F02C3/20
    • F01K23/062F02C3/205F23C6/04
    • A process and an arrangement are disclosed for operating a composite power station with a circulating fluidized bed furnace for solid fuels, in particular brown coal. The object of the invention is to recover and use combustion gas with high caloric values, i.e. to ensure an optimum post-combustion of the flue gas in order to achieve a maximum entrance temperature in the gas turbine. For that purpose, the flue gas partial current (15) is diverted in the substoichiometrically operated area of the fluidized bed furnace, upstream of the secondary air inlet (5), or the boiler is substoichiometrically operated as a carburetor and fresh air is added to the flue gas after the flue gas is cleaned and before it is subsequently burned. To implement this process, the combustion gas channel (15) is embedded in the substoichiometrically operated area of the fluidized bed furnace, upstream of the secondary air inlet (5), or the air channel is subdivised upstream of the boiler into controllable partial channels. One partial channel is embedded in the fluidized bed furnace and the other partial channel is embedded in the flue gas channel or in the post-combustion device.