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    • 11. 发明专利
    • Liquid fuel production plant
    • 液体燃料生产厂
    • JP2005336076A
    • 2005-12-08
    • JP2004154990
    • 2004-05-25
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • HIRABAYASHI TAKUYAMIYAMOTO HITOSHIWATABE MASAHARUNAKAMORI NOBUOMATSUMURA SATOSHIKODAMA JUNICHIROYAMAZAKI HISAHIRO
    • C07C29/151C07C31/04C07C41/09C07C43/06C10G3/00C10L1/02
    • Y02P30/20
    • PROBLEM TO BE SOLVED: To provide a liquid fuel production plant enabling a liquid fuel to be produced more than the conventional cases relative to the amount of a feedstock gas to be charged, and enabling continuous operation by continually stably heating a reformer, thus enabling the liquid fuel to be produced in high efficiency. SOLUTION: The liquid fuel production plant comprises the step S1 of charging a feedstock gas, the step S2 of removing substances unnecessary for the reforming step, the step S3 of reforming methane in the feedstock gas into a mixed gas comprising at least carbon dioxide and hydrogen among carbon monoxide, carbon dioxide and hydrogen, the step S4 of compressing the mixed gas and the step S5 of synthesizing methanol. In this plant, as part or the whole of heat necessary for reforming in the step S3, waste heat discharged from adjoining other plant(s) is utilized, and there is an auxiliary heating means 8 for supplementing the deficit of waste heat fed from the other plant(s). COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:为了提供一种液体燃料生产设备,其使液体燃料比常规的情况相对于待加料的原料气体的量更多地产生,并且能够通过连续稳定地加热重整器来连续运行, 从而能够高效率地制造液体燃料。 解决方案:液体燃料生产设备包括对原料气体进行充料的步骤S1,除去重整步骤所不需要的物质的步骤S2,将原料气体中的甲烷重整成包含至少碳的混合气体的步骤S3 一氧化碳,二氧化碳和氢气中的二氧化碳和氢气,压缩混合气体的步骤S4和合成甲醇的步骤S5。 在该工厂中,作为在步骤S3中重整所需的热量的一部分或全部,利用从相邻的其他设备排出的废热,并且存在辅助加热装置8,用于补充从 其他植物。 版权所有(C)2006,JPO&NCIPI
    • 13. 发明专利
    • REGENERATIVE STEAM PLANT
    • JPH0711915A
    • 1995-01-13
    • JP15340993
    • 1993-06-24
    • MITSUBISHI HEAVY IND LTD
    • NAKAMORI NOBUO
    • F01K3/14G21D5/08
    • PURPOSE:To compose a plant wherein heat of surplus steam is accumulated and is made heat-released as required. CONSTITUTION:A steam turbine 3 is driven by steam generated in a steam generator 1, and steam leaving the steam turbine is condensed by a condenser 4, then is heated in low and high pressure feed water heaters 7 and 12 to be fed to the steam generator. When electricity is surplus like in a height, part of main steam 2 to sent to the steam turbine is bled to reduce power generation quantity. Bled steam 14 is sent to a hydrogen storage utilizing heat accumulator 15 to heat and temperature-rise hydrogen storage alloy 16 to accumulate heat. Dehydrogenation reaction occurs in the hydrogen storage alloy 16 heated and temperature-risen, and this hydrogen is flowed in a hydrogen reservoir 18. When electricity is needed like in the daytime, part of feedwater to be sent to the steam generator is bypassed to a hydrogen storage alloy utilizing heat accumulator from the outlet of a feed water pump 11 and/or the outlet of a high-pressure feed water heater 12. Bypassing feed water 19 is heated to raise temperature at the heat accumulator to release accumulated heat to store hydrogen from a hydrogen reservoir.
    • 14. 发明专利
    • STEAM GENERATOR EQUIPPED WITH ECONOMIZER
    • JPH01318801A
    • 1989-12-25
    • JP15015688
    • 1988-06-20
    • MITSUBISHI HEAVY IND LTD
    • NAKAMORI NOBUOKAWANISHI KOHEITSUGE AYAOKUSAKABE TAKANARI
    • F22B1/16
    • PURPOSE:To increase the flow speed of feed water in the area of an economizer and improve heat transfer performance by arranging feed water flow speed increasing members between a plurality of heat transfer tubes in the area of the economizer. CONSTITUTION:Feed water flow speed increasing members 20 for increasing the flow speed of feed water 14 flowing through the area 9 of an economizer are arranged between heat transfer tubes 6 in the area 9 of the economizer. The feed water 14 flows through an annular passage 24, defined between the outer surfaces of respective heat transfer tubes 6 and the inner surface of a sleeve 21, as shown by an arrow sign 23 in a diagram and passes through the area 9 of the economizer to enter into boiling area. The flow speed of the feed water in the area of the economizer is increased by providing the flow speed increasing members between the heat transfer tubes in the area of the economizer in such a manner and, therefore, a heat transfer rate in secondary side is changed and a heat passing coefficient is increased whereby heat transfer performance may be improved.
    • 15. 发明专利
    • GAS-LIQUID SEPARATOR
    • JPS6233515A
    • 1987-02-13
    • JP17100985
    • 1985-08-02
    • MITSUBISHI HEAVY IND LTD
    • NAKAHARA TAKAFUMIHIRAO YASUHIKONAKAMORI NOBUOKOTO TOSHIYUKI
    • B04C3/00B01D45/08B01D45/12
    • PURPOSE:To obtain the titled compact and high-performance separator for a steam drum by colliding 2-phase stream at the outlet of a tangential nozzle of the outer cylinder and separating into a gaseous phase and a liq. phase and providing a collision plate for allowing the liq. separated by the corrugated separator to flow along its inner wall. CONSTITUTION:A tangential nozzle 2 is provided to an outer cylinder 1 and a separated liq. is discharged to reduce the flow velocity at the site. A collision plate 3 is furnished at the outlet of the tangential nozzle 2, the separated liq. is struck against the plate and gas and liq. are separated. The separated liq. is allowed to flow down along the collision plate 3 along with the separated liq. flowing out from a corrugated gas-liq. separator 9 and the free falling of the separated liq. at a high speed is prevented. Moreover, a liq. collecting dish 4 is provided and all the separated liq. is collected. The vertical downward vector of the separated liq. is nullified and the inrush of the separated liq. into the liq. surface at a high velocity is prevented.