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    Manufacture of charcoal
    1.
    发明授权
    Manufacture of charcoal 有权
    木炭制造

    公开(公告)号：US08303777B2

    公开(公告)日：2012-11-06

    申请号：US13474859

    申请日：2012-05-18

    申请人： Andrew Mark Elliott

    发明人： Andrew Mark Elliott

    IPC分类号： C10B49/02

    CPC分类号： C10G1/00 ,  C10B49/08 ,  C10B53/02 ,  Y02E50/14 ,  Y02P20/145

    摘要： Apparatus for the manufacture of charcoal, comprising a unit having walls defining a primary combustion chamber, and a material inlet for allowing a feed of wood chips though said material inlet into said apparatus. A trough is located at a lower height than said material inlet such that material passing through said material inlet is able to fall into the trough. An air inlet is located below the material inlet such that, when wood chips are located within the trough piled up to said material inlet, air passing from said air inlet passes through said wood-chips and into the primary combustion chamber.

    摘要翻译： 用于制造木炭的装置，包括具有限定初级燃烧室的壁的单元和用于允许通过所述材料入口进入所述装置的木屑进料的材料入口。 槽位于比所述材料入口更低的高度处，使得通过所述材料入口的材料能够落入槽中。 空气入口位于材料入口下方，使得当木片位于堆积到所述材料入口的槽内时，从所述空气入口通过的空气通过所述木屑并进入主燃烧室。

    PYROLYSER
    2.
    发明申请
    PYROLYSER 有权

    公开(公告)号：US20120125757A1

    公开(公告)日：2012-05-24

    申请号：US13383970

    申请日：2010-07-13

    申请人： Robert D. Eden

    发明人： Robert D. Eden

    IPC分类号： C10B49/02 ,  C10K1/02

    CPC分类号： C10B49/08 ,  C10B1/04 ,  C10B49/06 ,  C10B53/02 ,  C10J3/20 ,  C10J3/34 ,  C10J3/485 ,  C10J3/84 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/1253 ,  C10J2300/165 ,  C10J2300/1671 ,  C10K1/04 ,  Y02E50/14 ,  Y02P20/145

    摘要： The present invention provides a pyrolysis system comprising an entrained flow pyrolyser having an opening through which biomass can be added. The pyrolyser also has an inlet for hot exhaust gas, an outlet for pyrolysed biomass and an outlet for syngas. The system has a burner for producing hot exhaust gas and a conduit between the burner and the hot exhaust gas inlet. A syngas extraction means for extracting syngas from the pyrolyser. The syngas extraction means extracts syngas from the pyrolyser at a rate such that the internal pressure within the pyrolyser never exceeds the pressure external to the pyrolyser.

    摘要翻译： 本发明提供了一种包含夹带流动热解器的热解系统，其具有可以添加生物质的开口。 热解器还具有用于热废气的入口，用于热解生物质的出口和用于合成气的出口。 该系统具有用于产生热废气的燃烧器和燃烧器与热废气入口之间的导管。 一种用于从热解器中提取合成气的合成气提取装置。 合成气提取装置以使得热解器内的内部压力不超过热解器外部的压力的速率从热解器中提取合成气。

    Method of and apparatus for heat processing of pulverized solid fuel
    4.
    发明授权
    Method of and apparatus for heat processing of pulverized solid fuel 失效
    粉碎固体燃料的热处理方法和装置

    公开(公告)号：US4244700A

    公开(公告)日：1981-01-13

    申请号：US19663

    申请日：1979-03-12

    申请人： Zinovy F. Chukhanov ,  Zinovy Z. Chukhanov ,  Sergei A. Tsuprov ,  Vadim A. Karasev ,  Anatoly M. Nikolaev ,  Robert M. Shibaev ,  Boris F. Bratchenko ,  Ivan V. Lyashenko

    发明人： Zinovy F. Chukhanov ,  Zinovy Z. Chukhanov ,  Sergei A. Tsuprov ,  Vadim A. Karasev ,  Anatoly M. Nikolaev ,  Robert M. Shibaev ,  Boris F. Bratchenko ,  Ivan V. Lyashenko

    IPC分类号： C10B49/08 ,  C10G1/02 ,  C10L9/08 ,  C10L1/32

    CPC分类号： C10G1/02 ,  C10B49/08

    摘要： According to the invention pulverized solid fuel is processed by heating the fuel to a temperature at which thermal decomposition of the fuel begins and subsequently heating the fuel to a temperature at which an intense thermal decomposition of the fuel takes place to form a vapor-and-gas suspension containing pulverized particles, gas, tar vapors and pyrogenic water vapors. The resultant vapor-and-gas suspension is cooled in a chamber by water and/or pyrogenic water to a temperature from 360.degree. to 140.degree. C. at which pulverized solid particles adsorb heavy tar. To obtain the resulting product in the form of a pulp, the vapor-and-gas suspension is cooled for a second time to a temperature from 80.degree. to 20.degree. C. at which the fractures of intermediate and light tars are condensed.Combustion heat of resulting solid matter is higher than that of the product obtained by a conventional method; in addition, it may be conveyed by a water channel. The resulting product in the form of a pulp may be conveyed by a water channel directly to the consumer. When practising the method, such side product as pyrogenic water is utilized which is usually purified prior to disposal.

    摘要翻译： 根据本发明，粉碎的固体燃料通过将燃料加热到燃料热分解开始的温度并随后将燃料加热到发生燃料的强烈热分解的温度以形成蒸气 - 含有粉碎颗粒的气体悬浮液，气体，焦油蒸气和热原水蒸汽。 所得蒸汽和气体悬浮液在室内由水和/或热解水冷却至360℃至140℃的温度，在该温度下粉碎的固体颗粒吸附重质焦油。 为了得到纸浆形式的所得产物，将气 - 气悬浮液第二次冷却至80℃至20℃的温度，在此温度下中和轻焦油的断裂会凝结。 所得固体物质的燃烧热量高于通过常规方法获得的产品的燃烧热; 此外，它可以由水通道传送。 纸浆形式的所得产品可以通过水通道直接输送到消费者。 当实施该方法时，使用诸如热解水的副产物，其通常在处置之前进行纯化。

    Method and apparatus for the transfer of entrained solids
    5.
    发明授权
    Method and apparatus for the transfer of entrained solids 失效
    用于转移夹带固体的方法和设备

    公开(公告)号：US3874739A

    公开(公告)日：1975-04-01

    申请号：US38623173

    申请日：1973-08-07

    申请人： EXXON RESEARCH ENGINEERING CO

    发明人： MITCHELL WILLARD N

    IPC分类号： B01J8/00 ,  C10B49/08 ,  C10J3/50 ,  C10J3/54 ,  B65G53/04

    CPC分类号： C10J3/482 ,  B01J8/0025 ,  C10B49/08 ,  C10J3/503 ,  C10J3/723 ,  C10J3/78 ,  C10J3/84 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1606 ,  C10J2300/1807

    摘要： Solid particles are transferred from a standpipe or similar vessel in which a stream of particles moves downwardly in dense phase flow to a transfer line burner or other vessel in which the particles are carried upwardly in dilute phase flow by withdrawing the downwardly moving dense flow stream of particles from the first vessel, reducing the cross-sectional area of the stream of particles by a factor of from about 1.2 to about 10 while introducing sufficient gaseous fluid to maintain the particles in dense phase flow, directing the stream of particles of reduced cross-sectional area upwardly into the second vessel while injecting sufficient additional gaseous fluid upwardly into the stream of particles to aerate the particles without producing dilute phase flow, and thereafter introducing additional gaseous fluid upwardly into the second vessel in a quantity sufficient to produce a rapid transition from dense phase flow to dilute phase flow.

    摘要翻译： 固体颗粒从立管或类似的容器转移，其中颗粒物流在致密相流中向下移动到传输线燃烧器或其它容器中，其中颗粒在稀相流中向上运送，通过撤回向下移动的稠流流 来自第一容器的颗粒，将颗粒流的横截面面积减小约1.2至约10倍，同时引入足够的气态流体以保持颗粒处于致密相流动， 截面积向上进入第二容器，同时将足够的附加气态流体向上注入到颗粒物流中以使颗粒通气而不产生稀相流，然后将额外的气态流体向上引入第二容器中，其量足以产生从 稠相流稀相流。

    Coal carbonizing in trickling streams
    6.
    发明授权
    Coal carbonizing in trickling streams 失效
    煤层气中的煤炭碳化

    公开(公告)号：US3705086A

    公开(公告)日：1972-12-05

    申请号：US3705086D

    申请日：1970-07-07

    申请人： METALLGESELLSCHAFT AG

    发明人： SCHMALFELD PAUL ,  HAHN HELMUT

    IPC分类号： C10B49/04 ,  C10B49/08 ,  C10B47/20

    CPC分类号： C10B49/08

    摘要： FINE-GRAINED COKE IS PRODUCED BY A CARBONIZATION OF FINE-GRAINED COAL BY A TREATMENT WITH A HOT GAS. THE COAL TRICKLES DOWN IN A COUNTERCURRENT TO THE RISING HOT GAS PAST FIXTURES WHICH RETARD THE FREE FALL AND OCCUPY UP TO 50% OF THE CROSS-SECTION OF THE FLOW. THE COAL MAY IN THAT WAY BE MADE SUITABLE FOR USE IN MAKING BRIQUETTES.