Device and method for generating a synthesis gas from processed biomass by entrained-flow gasification
    11.
    发明授权
    Device and method for generating a synthesis gas from processed biomass by entrained-flow gasification 有权
    通过夹带气化从处理的生物质产生合成气的装置和方法

    公开(公告)号:US08603204B2

    公开(公告)日:2013-12-10

    申请号:US13511243

    申请日:2010-11-26

    Abstract: 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.

    Abstract translation: 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。

    Fuel preparation
    12.
    发明授权
    Fuel preparation 有权
    燃料准备

    公开(公告)号:US07972392B2

    公开(公告)日:2011-07-05

    申请号:US12095978

    申请日:2006-11-03

    CPC classification number: C10L1/026 Y02E50/13

    Abstract: The invention relates to a fuel preparation for use in diesel engines consisting of plant oil mono-alcohol esters and up to 20 weight percent linear and branched paraffins and olefins of chain length C5-C11 and alcohols of chain length C2-C8, whereby the paraffins, olefins and alcohols are obtained by means of gasification of biomass and subsequent Fischer-Tropsch synthesis not involving any processing of the Fischer-Tropsch fraction by means of hydrogenating procedures and the preparation has a flash point >55° C. and a density >820 kg/m3.

    Abstract translation: 本发明涉及一种用于柴油发动机的燃料制备装置,其由植物油单醇酯和至多20重量%的直链和支链烷烃和链长C5-C11的烯烃和链长C2-C8的醇组成,其中链烷烃 ,烯烃和醇通过生物质的气化和随后的费 - 托合成而获得,不涉及通过氢化方法对费 - 托馏分的任何处理,并且制备的闪点> 55℃,密度> 820 kg / m3。

    Process and apparatus for the endothermic gasification of carbon
    15.
    发明授权
    Process and apparatus for the endothermic gasification of carbon 有权
    碳吸热气化的工艺和装置

    公开(公告)号:US07776114B2

    公开(公告)日:2010-08-17

    申请号:US11460379

    申请日:2006-07-27

    Abstract: A process for the endothermic gasification of solid carbon in an entrained bed facility comprises partial oxidation of fuel(s) and endothermic gasification of solid carbon, preferably preceded by low temperature carbonization such that the carbonization gas is passed to the partial oxidation and the carbonization coke is passed to the endothermic gasification. The hot gas streaming downwardly from the combustion chamber is deflected to produce separation of the liquid slag and is then passed to the endothermic gasification that operates with a rising gas stream and with addition of solid carbon having a grain diameter of up to 20 mm. The speed of the gas at the carbon inlet is higher than, and the speed of the gas at the end of the endothermic gasification is lower than, the suspension rate of the reactive carbon particles, to produce an increase of the relative speed difference between the gas and the carbon particles. Apparatus is also disclosed for carrying out the process.

    Abstract translation: 在夹带床设备中固体碳的吸热气化的方法包括燃料的部分氧化和固体碳的吸热气化,优选在低温碳化之前,使得碳化气体进入部分氧化和碳化焦炭 被传递到吸热气化。 从燃烧室向下流动的热气体被偏转以产生液体炉渣的分离,然后被传递到用升高的气流运行的吸热气化,并加入具有高达20mm的粒径的固体碳。 碳入口处的气体速度高于吸热气化结束时的气体速度低于反应性碳颗粒的悬浮速度,以产生相对速度差 气体和碳颗粒。 还公开了用于执行该过程的装置。

    Fuel Preparation
    16.
    发明申请
    Fuel Preparation 有权
    燃料准备

    公开(公告)号:US20080295396A1

    公开(公告)日:2008-12-04

    申请号:US12095978

    申请日:2006-11-03

    CPC classification number: C10L1/026 Y02E50/13

    Abstract: The invention relates to a fuel preparation for use in diesel engines consisting of plant oil mono-alcohol esters and up to 20 weight percent linear and branched paraffins and olefins of chain length C5-C11 and alcohols of chain length C2-C8, whereby the paraffins, olefins and alcohols are obtained by means of gasification of biomass and subsequent Fischer-Tropsch synthesis not involving any processing of the Fischer-Tropsch fraction by means of hydrogenating procedures and the preparation has a flash point >55° C. and a density >820 kg/m3.

    Abstract translation: 本发明涉及一种用于柴油发动机的燃料制备装置,其由植物油单醇酯和至多20重量%的直链和支链烷烃和链长C5-C11的烯烃和链长C2-C8的醇组成,其中链烷烃 ,烯烃和醇通过生物质的气化和随后的费 - 托合成而获得,不涉及通过氢化方法对费 - 托馏分的任何处理,并且制备的闪点> 55℃,密度> 820 kg / m3。

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