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    METHOD OF MAKING SYNGAS AND APPARATUS THEREFOR
    93.
    发明申请
    METHOD OF MAKING SYNGAS AND APPARATUS THEREFOR 失效
    制作方法及其设备

    公开(公告)号：US20100276641A1

    公开(公告)日：2010-11-04

    申请号：US12768841

    申请日：2010-04-28

    Applicant: James Klepper

    Inventor： James Klepper

    IPC: C01B3/34 ,  B01J19/00

    CPC classification number: B01J7/00 ,  C10J3/485 ,  C10J3/506 ,  C10J3/526 ,  C10J3/84 ,  C10J2200/152 ,  C10J2200/158 ,  C10J2300/092 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1215 ,  C10J2300/1253 ,  C10K1/026

    Abstract: Syngas is formed by combining a carbon source with steam at an elevated temperature in a generally horizontal reactor. The heat for the reaction is provided by a stoichiometric combustion nozzle at a first end of the horizontal reaction chamber. The carbon source is deposited downwardly into the reaction chamber where it combines with a flowing stream of hot gas formed from the stoichiometric combustion in combination with steam and additional oxygen, if necessary. This flowing stream of gas reacts with the deposited carbon feed source and is directed to a cyclone separator where the formed syngas is recovered from an upper portion of the separator and any formed ash is directed into a collection tank.

    Abstract translation: 合成气通过在大体上水平的反应器中在升高的温度下将碳源与蒸汽组合而形成。 用于反应的热量由化学计量燃烧喷嘴在水平反应室的第一端提供。 如果需要，将碳源向下沉积到反应室中，其中它与由化学计量燃烧形成的热气合流与蒸汽和额外的氧组合。 这种流动的气流与沉积的碳进料源反应并被引导到旋风分离器，其中形成的合成气从分离器的上部回收并且任何形成的灰分被引导到收集罐中。

    Process for converting carbon dioxide from coal utilization to a solid ash
    98.
    发明申请
    Process for converting carbon dioxide from coal utilization to a solid ash 有权
    将二氧化碳从煤炭利用转化为固体灰的工艺

    公开(公告)号：US20100178239A1

    公开(公告)日：2010-07-15

    申请号：US12684177

    申请日：2010-01-08

    Applicant: Udo von Wimmersperg ,  Laurinel Owen

    Inventor： Udo von Wimmersperg ,  Laurinel Owen

    IPC: C01B3/02

    CPC classification number: C10J3/00 ,  C10J3/485 ,  C10J3/84 ,  C10J2300/093 ,  C10J2300/0976 ,  C10J2300/0983 ,  C10J2300/0996 ,  C10J2300/1646 ,  C10J2300/165 ,  C10J2300/1671 ,  C10J2300/1853 ,  C10K1/024 ,  H01M8/0643 ,  Y02P70/56

    Abstract: A process for conversion of coal in a reaction vessel comprises steps of: admixing coal and powdered alumina clay to form reactants; injecting the reactants with a high-pressure steam jet into the reaction vessel; and producing aluminum oxalate ash and hydrogen. Preferably, the reaction vessel is pressurized to maximize the production of aluminum oxalate and hydrogen. Optionally, the process includes adding calcium carbonate if not present in the clay. The reactants in the reaction vessel are typically maintained a temperature of about 2,000 degrees Kelvin and a pressure of about 1 mega Pascals. To save energy, the process may include preheating water with the aluminum oxalate ash to aid in creating pressurized steam. The hydrogen may be mixed with air and burned in a combustion chamber, such as is found within a gas turbine-generator unit to produce electricity. Optionally the reactants may include an aqueous sodium hydroxide.

    Abstract translation: 在反应容器中转化煤的方法包括以下步骤：混合煤和氧化铝粉末形成反应物; 将反应物用高压蒸汽喷射注入反应容器中; 并生产草酸铝灰和氢。 优选地，将反应容器加压以使草酸铝和氢气的产生最大化。 任选地，该方法包括如果不存在于粘土中则添加碳酸钙。 反应容器中的反应物通常保持约2000开氏温度和约1兆帕斯卡的压力。 为了节省能源，该方法可以包括用草酸铝灰预热水以帮助产生加压蒸汽。 氢气可以与空气混合并在燃烧室中燃烧，例如在燃气涡轮发电机单元内发现以产生电力。 任选地，反应物可以包括氢氧化钠水溶液。

    TAR-FREE GASIFICATION SYSTEM AND PROCESS
    100.
    发明申请
    TAR-FREE GASIFICATION SYSTEM AND PROCESS 有权
    无油气化系统和工艺

    公开(公告)号：US20100155669A1

    公开(公告)日：2010-06-24

    申请号：US12635244

    申请日：2009-12-10

    Applicant: Albert C. Tsang ,  David L. Breton

    Inventor： Albert C. Tsang ,  David L. Breton

    IPC: C10J3/48 ,  C10J3/46

    CPC classification number: C10J3/56 ,  C10J3/485 ,  C10J3/721 ,  C10J3/74 ,  C10J3/78 ,  C10J3/84 ,  C10J3/845 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1807 ,  C10J2300/1846

    Abstract: A novel tar-free gasification process and system is disclosed that involves the partial combustion of recycled dry solids and the drying of a slurry feedstock comprising carbonaceous material in two separate reactor zones in a two stage gasifier, thereby producing mixture products comprising synthesis gas. The synthesis gas produced from the high temperature first stage reaction zone is then quenched in the second stage reaction zone of the gasifier prior to introduction of a slurry feedstock. The temperature of the final syngas exiting the second stage reaction zone of the gasifier is thereby moderated to be in the range of about 350-900° F., which is below the temperature range at which tar is readily formed, depending upon the type of carbonaceous feedstock utilized.

    Abstract translation: 公开了一种新颖的无焦油气化方法和系统，其涉及再循环的干固体的部分燃烧和在两级气化器中的两个分离的反应器区域中包含碳质材料的浆料原料的干燥，从而产生包含合成气的混合物。 然后在引入浆料原料之前，从高温第一阶段反应区产生的合成气在气化器的第二阶段反应区骤冷。 因此，离开气化器的第二阶段反应区的最终合成气的温度被调节到约350-900°F的范围内，该温度低于焦油容易形成的温度范围，这取决于 使用碳质原料。

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