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    APPARATUS FOR COMBUSTING A FUEL AT HIGH PRESSURE AND HIGH TEMPERATURE, AND ASSOCIATED SYSTEM
    34.
    发明申请
    APPARATUS FOR COMBUSTING A FUEL AT HIGH PRESSURE AND HIGH TEMPERATURE, AND ASSOCIATED SYSTEM 有权
    用于燃烧高压和高温燃料的装置及相关系统

    公开(公告)号：US20110083435A1

    公开(公告)日：2011-04-14

    申请号：US12872364

    申请日：2010-08-31

    申请人： Miles R. Palmer ,  Rodney John Allam ,  Glenn William Brown, JR.

    发明人： Miles R. Palmer ,  Rodney John Allam ,  Glenn William Brown, JR.

    IPC分类号： F02C1/00 ,  F23D1/00 ,  F23L7/00 ,  F02C3/20

    CPC分类号： F23D1/00 ,  B01D53/34 ,  B01J19/00 ,  F23G7/065 ,  F23J15/027 ,  F23L7/002 ,  F23L7/007 ,  F23L2900/07001 ,  F23L2900/07002 ,  F23L2900/07003 ,  F23L2900/07007 ,  F23L2900/07008 ,  F23M5/08 ,  F23M2900/05004 ,  F23R3/002 ,  F23R2900/03041 ,  Y02E20/12 ,  Y02E20/322 ,  Y02E20/344

    摘要： A combustor apparatus is provided, comprising a mixing arrangement for mixing a carbonaceous fuel with enriched oxygen and a working fluid to form a fuel mixture. A combustion chamber is at least partially defined by a porous perimetric transpiration member, at least partially surrounded by a pressure containment member. The combustion chamber has longitudinally spaced apart inlet and outlet portions. The fuel mixture is received by the inlet portion for combustion within the combustion chamber at a combustion temperature to form a combustion product. The combustion chamber further directs the combustion product longitudinally toward the outlet portion. The porous transpiration member is configured to substantially uniformly direct a transpiration substance laterally therethrough, about the perimeter thereof defining the combustion chamber and longitudinally between the inlet and outlet portions, toward the combustion chamber for buffering interaction between the combustion product and the porous transpiration member. Associated systems are also provided.

    摘要翻译： 提供了一种燃烧器装置，其包括用于混合含碳燃料和富氧的混合装置和工作流体以形成燃料混合物。 燃烧室至少部分地由多孔周边蒸腾构件限定，至少部分地被压力容纳构件包围。 燃烧室具有纵向间隔开的入口和出口部分。 燃料混合物被入口部分接收以在燃烧室内在燃烧温度下燃烧以形成燃烧产物。 燃烧室进一步将燃烧产物纵向引向出口部分。 多孔蒸腾构件被构造成基本上均匀地引导蒸发物质围绕其限定燃烧室的周边并且纵向在入口部分和出口部分之间横向通过其朝向燃烧室缓冲燃烧产物和多孔蒸腾构件之间的相互作用。 还提供了相关系统。

    Apparatus for Upgrading Heavy Hydrocarbons Using Supercritical Water
    38.
    发明申请
    Apparatus for Upgrading Heavy Hydrocarbons Using Supercritical Water 审中-公开
    使用超临界水升级重质烃的设备

    公开(公告)号：US20100189610A1

    公开(公告)日：2010-07-29

    申请号：US12754865

    申请日：2010-04-06

    申请人： Rodney John Allam

    发明人： Rodney John Allam

    IPC分类号： B01J19/00

    CPC分类号： B01J3/008 ,  B01F5/0604 ,  B01J19/0053 ,  B01J2219/00006 ,  B01J2219/00777 ,  C10G9/38 ,  C10J3/80 ,  C10J2300/0979 ,  C10J2300/0989 ,  Y02P20/544

    摘要： Heavy hydrocarbons are upgraded more efficiently to lighter, more valuable, hydrocarbons with lower amounts of solid carbonaceous by-products in supercritical water using two heating stages, the first stage at a temperature up to about 775K and the second stage at a temperature from about 870K to about 1075K. The temperature is preferably raised from the first temperature to the second temperature by internal combustion using oxygen.

    摘要翻译： 使用两个加热阶段，将重质烃更有效地升级至更轻，更有价值的含有较少量固体碳质副产物的超临界水，第一阶段在高达约775K的温度下，第二阶段在约870K温度 至约1075K。 温度优选通过使用氧的内燃从第一温度升高到第二温度。

    PROCESS AND APPARATUS FOR UPGRADING COAL USING SUPERCRITICAL WATER
    39.
    发明申请
    PROCESS AND APPARATUS FOR UPGRADING COAL USING SUPERCRITICAL WATER 审中-公开
    使用超级水提升煤的工艺和装置

    公开(公告)号：US20090206007A1

    公开(公告)日：2009-08-20

    申请号：US12033961

    申请日：2008-02-20

    申请人： Rodney John Allam

    发明人： Rodney John Allam

    IPC分类号： C10G1/00 ,  B01J19/00

    CPC分类号： B01J3/008 ,  B01F5/0659 ,  B01J2219/00006 ,  B01J2219/00777 ,  C10G1/047 ,  C10J3/80 ,  C10J2300/093 ,  C10J2300/0979 ,  Y02E20/16 ,  Y02P20/544

    摘要： Coal is converted into hydrocarbon compounds using supercritical water. The process involves two stages; a first stage in which carbonaceous material is reacted with supercritical water at above 850K to produce a first supercritical fluid reaction mixture comprising hydrocarbon compounds; and a second stage in which hydrocarbon compounds are extracted from coal mixed with at least a portion of the first supercritical fluid at a temperature within a range of from the supercritical temperature of water to about 695K. Char from the second stage is finely divided and may be either be used outside the process, e.g. in a coal fired power station or a gasifier, or used as at least a portion of the carbonaceous material used in the first stage.

    摘要翻译： 使用超临界水将煤转化成烃化合物。 该过程涉及两个阶段; 第一阶段，其中碳质材料与超过850K的超临界水反应以产生包含烃化合物的第一超临界流体反应混合物; 以及在从超临界温度至约695K的范围内的温度下，从与第一超临界流体的至少一部分混合的煤中提取烃化合物的第二阶段。 来自第二阶段的炭被细分，可以在工艺外使用，例如 在燃煤发电厂或气化炉中，或用作第一阶段中使用的至少一部分碳质材料。

    Purification of Carbon Dioxide
    40.
    发明申请
    Purification of Carbon Dioxide 有权
    二氧化碳的净化

    公开(公告)号：US20080226515A1

    公开(公告)日：2008-09-18

    申请号：US12129763

    申请日：2008-05-30

    申请人： Rodney John Allam ,  Vincent White ,  Edwin John Miller

    发明人： Rodney John Allam ,  Vincent White ,  Edwin John Miller

    IPC分类号： B01D53/56 ,  B01D53/50

    CPC分类号： B01D53/60 ,  B01D2257/302 ,  B01D2257/404 ,  C01B32/50 ,  Y02A50/2344 ,  Y02A50/2349 ,  Y02C10/14 ,  Y02P20/152

    摘要： SO2 and/or NOx are removed from gaseous CO2 at elevated pressure(s) in the presence of molecular oxygen and water and, when SO2 is to be removed, NOx, to convert SO2 to sulfuric acid and/or NOx to nitric acid. The sulfuric acid and/or nitric acid is/are then removed from the gaseous carbon dioxide to produce SO2-free, NOx-lean carbon dioxide gas. The invention has particular application in the removal of SO2 and/or NOx from carbon dioxide flue gas produced in an oxyfuel combustion process, for example, in a pulverized coal fired power station.

    摘要翻译： 在分子氧和水的存在下，在升高的压力下从气态CO 2 2中除去SO 2和/或NO x x， 当要除去SO 2的情况下，将SO 2 SO 2转化为硫酸和/或NO 2 x N 2 >硝酸。 然后从气态二氧化碳中除去硫酸和/或硝酸以产生无SO 2，无水二氧化碳气体。 本发明特别适用于在氧燃料燃烧过程中产生的二氧化碳烟道气中除去SO 2和/或NO x 2，例如在粉煤燃烧 发电厂。