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    • 2. 发明申请
    • Process for the holding operation of a Fischer-Tropsch synthesis
    • 费 - 托合成的保持操作方法
    • US20070093560A1
    • 2007-04-26
    • US11584755
    • 2006-10-23
    • Anton AlthappBodo WolfDietmar RugerOlaf Schulze
    • Anton AlthappBodo WolfDietmar RugerOlaf Schulze
    • C07C27/26
    • C10G2/32
    • During required change-over to a holding operation in a Fischer-Tropsch synthesis, the reactor is not depressurized after cutting off the supply of fresh synthesis gas to the Fischer-Tropsch reactor, and the temperature is not reduced to below the temperature below which a Fischer-Tropsch reaction no longer takes place. Instead, the reactor is charged with an inert gas, e.g., kept in a vessel at a pressure higher than the operating pressure of the Fischer-Tropsch synthesis, until the reacting components have been flushed out from the Fischer-Tropsch system. While maintaining the pressure and the temperature, the reactor is thus merely inerted for a few seconds, sufficient to interrupt the Fischer-Tropsch reaction. Catalyst damage is avoided, and the liquid phase situation on the catalyst is at least essentially unchanged, facilitating subsequent re-commissioning of the catalyst.
    • 在需要转换为费 - 托合成中的保持操作期间,在切断向费 - 托反应器的新鲜合成气供应之后,反应器不会减压,并且温度不降低到低于该温度 费 - 托反应不再发生。 相反,反应器装有惰性气体,例如保持在容器中的压力高于费 - 托合成的操作压力,直至反应组分从费 - 托系统中冲出。 在保持压力和温度的同时,反应器仅仅被惰化几秒钟,足以中断费 - 托反应。 避免催化剂损伤,并且催化剂上的液相状况至少基本不变,有助于随后重新调试催化剂。
    • 3. 发明授权
    • Device and method for generating a synthesis gas from processed biomass by entrained-flow gasification
    • 通过夹带气化从处理的生物质产生合成气的装置和方法
    • US08603204B2
    • 2013-12-10
    • US13511243
    • 2010-11-26
    • Dietmar RügerOlaf SchulzeAnton AlthappChristian EichhornHorst Kretschmer
    • Dietmar RügerOlaf SchulzeAnton AlthappChristian EichhornHorst Kretschmer
    • B01J7/00C01B3/36C01B6/24C10J3/00C10J3/08
    • C10L5/44C10B53/02C10J3/466C10J3/485C10J3/66C10J3/84C10J2200/15C10J2300/0903C10J2300/0906C10J2300/0909C10J2300/0916C10L5/366C10L9/086Y02E50/10Y02E50/14Y02E50/30Y02P20/145
    • The present invention relates to a device for generating a synthesis gas (SG) from biomass (BM) by entrained-flow gasification. The device comprises a treatment plant (1), in which the biomass (BM) is supplied to a coarse crushing device (2), which is connected downstream via a first lock (3) to a pressurized carbonization plant (4) for the hydrothermal generation of carbonization char (KK) from the biomass (BM). The carbonization plant (4) comprises at least one preheating device (5) and a carbonization reactor (6) arranged downstream of the preheating device (5) and is connected downstream via a second lock (11) to at least one solid-liquid separation device (12, 13) for providing a fuel. A drying device (16) for drying the fuel is provided downstream of the solid-liquid separation device (12, 13), with a crushing device (18) for crushing the fuel to form pulverized fuel (BS) having particle sizes in the range of 55 μm to 500 μm being connected downstream of the drying device. The device further comprises a transfer device (21) for transferring the fuel to an entrained-flow gasification plant (22), whereby a coupling of the treatment plant (1) to the entrained-flow gasification plant (22) is provided. The present invention further relates to a method for generating a synthesis gas (SG) from biomass (BM) by entrained-flow gasification using a device according to the invention.
    • 本发明涉及通过夹带气化从生物质(BM)产生合成气(SG)的装置。 该设备包括处理设备(1),其中生物质(BM)被供应到粗粉碎设备(2),其通过第一锁(3)连接到下游,到用于水热的加压碳化设备(4) 从生物量(BM)产生碳化焦炭(KK)。 碳化装置(4)包括布置在预热装置(5)下游的至少一个预热装置(5)和碳化反应器(6),并通过第二锁定件(11)连接到下游,至少一个固液分离 装置(12,13),用于提供燃料。 用于干燥燃料的干燥装置(16)设置在固液分离装置(12,13)的下游,具有用于破碎燃料的破碎装置(18),以形成粒度在该范围内的粉碎燃料(BS) 55毫米至500毫米的连接在干燥装置的下游。 该装置还包括用于将燃料转移到夹带气化装置(22)的转移装置(21),由此提供处理装置(1)与夹带气化装置(22)的联接。 本发明还涉及通过使用根据本发明的装置的夹带气化从生物质(BM)产生合成气(SG)的方法。
    • 5. 发明申请
    • DEVICE AND METHOD FOR GENERATING A SYNTHESIS GAS FROM PROCESSED BIOMASS BY ENTRAINED-FLOW GASIFICATION
    • 通过加入流化学气化从加工生物量产生合成气的装置和方法
    • US20120280181A1
    • 2012-11-08
    • US13511243
    • 2010-11-26
    • Dietmar RügerOlaf SchulzeAnton AlthappChristian EichhornHorst Kretschmer
    • Dietmar RügerOlaf SchulzeAnton AlthappChristian EichhornHorst Kretschmer
    • C01B3/02B01J7/00
    • C10L5/44C10B53/02C10J3/466C10J3/485C10J3/66C10J3/84C10J2200/15C10J2300/0903C10J2300/0906C10J2300/0909C10J2300/0916C10L5/366C10L9/086Y02E50/10Y02E50/14Y02E50/30Y02P20/145
    • The present invention relates to a device for generating a synthesis gas (SG) from biomass (BM) by entrained-flow gasification. The device comprises a treatment plant (1), in which the biomass (BM) is supplied to a coarse crushing device (2), which is connected downstream via a first lock (3) to a pressurized carbonization plant (4) for the hydrothermal generation of carbonization char (KK) from the biomass (BM). The carbonization plant (4) comprises at least one preheating device (5) and a carbonization reactor (6) arranged downstream of the preheating device (5) and is connected downstream via a second lock (11) to at least one solid-liquid separation device (12, 13) for providing a fuel. A drying device (16) for drying the fuel is provided downstream of the solid-liquid separation device (12, 13), with a crushing device (18) for crushing the fuel to form pulverized fuel (BS) having particle sizes in the range of 55 μm to 500 μm being connected downstream of the drying device. The device further comprises a transfer device (21) for transferring the fuel to an entrained-flow gasification plant (22), whereby a coupling of the treatment plant (1) to the entrained-flow gasification plant (22) is provided. The present invention further relates to a method for generating a synthesis gas (SG) from biomass (BM) by entrained-flow gasification using a device according to the invention.
    • 本发明涉及通过夹带气化从生物质(BM)产生合成气(SG)的装置。 该设备包括处理设备(1),其中生物质(BM)被供应到粗粉碎设备(2),其通过第一锁(3)连接到下游,到用于水热的加压碳化设备(4) 从生物量(BM)产生碳化焦炭(KK)。 碳化装置(4)包括布置在预热装置(5)下游的至少一个预热装置(5)和碳化反应器(6),并通过第二锁定件(11)连接到下游,至少一个固液分离 装置(12,13),用于提供燃料。 用于干燥燃料的干燥装置(16)设置在固液分离装置(12,13)的下游,具有用于破碎燃料的破碎装置(18),以形成粒度在该范围内的粉碎燃料(BS) 55μm至500μm的干燥装置连接在干燥装置的下游。 该装置还包括用于将燃料转移到夹带气化装置(22)的转移装置(21),由此提供处理装置(1)与夹带气化装置(22)的联接。 本发明还涉及通过使用根据本发明的装置的夹带气化从生物质(BM)产生合成气(SG)的方法。