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    • 2. 发明专利
    • COMBINED POWER GENERATION PLANT FOR EXHAUST RE- COMBUSTION
    • JP2000018010A
    • 2000-01-18
    • JP18604998
    • 1998-07-01
    • MITSUBISHI HEAVY IND LTD
    • MOMOTAKE CHIKANORIKANBARA MASAMICHI
    • F01K23/10
    • PROBLEM TO BE SOLVED: To reduce a capacity of a circulating water pump in a circulation line of an exhaust gas feed water heater, and improve controllability by arranging a plurality of feed water lines for the exhaust gas feed water heater as well as arranging a gas turbine, a steam turbine, and the like, and switching the feed water lines used according to a load condition. SOLUTION: Fuel is burnt by a gas turbine 1, power is generated in association with its rotation, waste heat from the gas turbine 1 is recovered by an exhaust re-combustion boiler 2, and steam turbines 3 to 6 are rotated so as to generate power. In this time, in a low pressure gas feed water heater 11 connected to a gas line 8 from the exhaust re-combustion boiler 2, water supplied from a condenser 55 is circulated by a circulation pump 59, and is discharged from a feed water line 81 to a feed water line 58. In a high pressure gas feed water heater 10, water supplied from the condenser 55 is circulated by a circulation pump 60, and is discharged from a feed water line 84 to the feed water line 58. Either one of each valve 101 to 103 is opened according to a load condition, and taking-out line for circulation water is changed.
    • 6. 发明专利
    • Power generation system
    • 发电系统
    • JP2005299576A
    • 2005-10-27
    • JP2004119541
    • 2004-04-14
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • MOMOTAKE CHIKANORI
    • F02C7/143F02C7/045F02C7/05F02C7/08
    • PROBLEM TO BE SOLVED: To suppress the occurrence of liquid moisture in a system in which a moisture remover is not interposed between an eliminator and a compressor.
      SOLUTION: This power generation system comprises a first heat exchanger 1, the eliminator 2 disposed on the downstream side of the first heat exchanger and removing the moisture and a second heat exchanger 3 disposed on the downstream side of the eliminator. The first temperature of an air reduced in temperature in the first heat exchanger 1 and passed through the first heat exchanger 1 is presented by T1 (the minimum value of T1 in the figure), and the second temperature of the air after the air is passed through the second heat exchanger 3 is presented by T2. A relation between the first temperature T1 and the second temperature T2 is set to T1
    • 要解决的问题:为了抑制在除气器和压缩机之间没有插入除湿器的系统中的液体水分的发生。 解决方案:该发电系统包括第一热交换器1,设置在第一热交换器的下游侧并除去水分的消除器2和设置在消除器的下游侧的第二热交换器3。 在第一热交换器1中通过第一热交换器1的温度降低的第一温度由T1(图中的T1的最小值)表示,空气通过后的空气的第二温度 通过第二热交换器3由T2呈现。 第一温度T1和第二温度T2之间的关系被设定为T1
    • 10. 发明专利
    • THERMAL ELECTRIC POWER PLANT
    • JPH11270354A
    • 1999-10-05
    • JP7153698
    • 1998-03-20
    • MITSUBISHI HEAVY IND LTD
    • KANBARA MASAMICHINISHIMURA ISAOMOMOTAKE CHIKANORISHIBATA MASATOSHI
    • F02C7/22C10G7/06C10G9/40F23C6/04
    • PROBLEM TO BE SOLVED: To improve the power generating efficiency while effectively utilizing the high-temperature exhaust gas to be generated in a heavy fuel oil heating and decomposing device or a raw oil heating and fractional distillation device by providing a route for feeding the exhaust gas generated by the combustion of the light gas from a heavy fuel oil decomposing unit in a heavy fuel oil heating and decomposing device to a boiler. SOLUTION: A heavy fuel oil decomposing unit (raw oil fractional distillation unit) including a heavy fuel oil heating and decomposing device (raw oil heating and fractional distillation device) 1, a gas turbine 2 and a boiler 3 are included as main equipment. Especially, a line 20 for feeding the exhaust gas to be generated by combustion of the light gas from the raw oil fractional distillation unit in the raw oil heating and fractional distillation device 1 to a boiler 3 is provided. Heat recovery in the boiler 3 is aimed at by this line 20. The exhaust gas from the raw oil heating and fractional distillation device 1 maintains the predetermined temperature, and efficiency can be remarkably raised by recovering the heat. Furthermore, since a desulfurizer and an NOx removal system in the downstream of the boiler 3 can be utilized, necessity of providing other desulfurizer and NOx removal system dedicated to the raw oil heating and fractional distillation device 1 is eliminated.