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    GAS DISTRIBUTOR FOR A ROTARY KILN
    2.
    发明申请
    GAS DISTRIBUTOR FOR A ROTARY KILN 审中-公开

    公开(公告)号：US20170137728A1

    公开(公告)日：2017-05-18

    申请号：US15419322

    申请日：2017-01-30

    申请人： Simple Approach Systems, Inc.

    发明人： Amirali G. Rehmat

    IPC分类号： C10J3/00 ,  F23L7/00 ,  C01B3/02 ,  F27B7/36

    CPC分类号： C10J3/005 ,  C01B3/02 ,  C10J2200/152 ,  C10J2300/0916 ,  C10J2300/0946 ,  F23L7/00 ,  F27B7/36 ,  Y10T137/85938

    摘要： A rotating air distributor for rotary reactors such as rotary kilns for the gasification of biomass and other carbonaceous materials for efficient mixing and maximum conversion of solid biomass and other carbonaceous materials into synthesis fuel gas is disclosed. The invention includes a gas distribution port comprises of one main supply from which several discharge nozzles emerge at different angles and at different locations along the length of the reactor to provide distribution of gas throughout the intended length of the reactor. The discharge of gas from the gas distribution port is adjusted by the variable position of a plug inside the port that can be adjusted during the operation of the kiln to achieve optimum gas-solid interaction along the length of the reactor. The rotating action of the gas distribution port also facilitates and eases the passage of reacted biomass solid and other carbonaceous material residue through the reactor.

    Method and apparatus for steam hydro-gasification with increased conversion times
    7.
    发明申请
    Method and apparatus for steam hydro-gasification with increased conversion times 有权
    蒸汽加氢气化方法和装置，转化时间越长

    公开(公告)号：US20080312348A1

    公开(公告)日：2008-12-18

    申请号：US12218653

    申请日：2008-07-16

    申请人： Chan Seung Park ,  Joseph M. Norbeck

    发明人： Chan Seung Park ,  Joseph M. Norbeck

    IPC分类号： C07C27/06 ,  B01J8/24

    CPC分类号： C01B3/34 ,  C01B2203/0233 ,  C01B2203/062 ,  C01B2203/0838 ,  C01B2203/1241 ,  C01B2203/148 ,  C01B2203/84 ,  C10G2/332 ,  C10G2300/1003 ,  C10G2300/1011 ,  C10G2300/201 ,  C10G2300/807 ,  C10J3/005 ,  C10J3/463 ,  C10J3/503 ,  C10J2300/093 ,  C10J2300/0966 ,  C10J2300/0973 ,  C10J2300/1246 ,  C10J2300/1659 ,  C10K3/00 ,  Y02E20/18 ,  Y02P30/20

    摘要： A method and apparatus for converting carbonaceous material to a stream of carbon rich gas, comprising heating a slurry feed containing the carbonaceous material in a hydrogasification process using hydrogen and steam, at a temperature and pressure sufficient to generate a methane and carbon monoxide rich stream in which the conversion time in the process is between 5 and 45 seconds. In particular embodiments, the slurry feed containing the carbonaceous material is fed, along with hydrogen, to a kiln type reactor before being fed to the fluidized bed reactor. Apparatus is provided comprising a kiln type reactor, a slurry pump connected to an input of the kiln type reactor, means for connecting a source of hydrogen to an input of the kiln type reactor; a fluidized bed reactor connected to receive output of the kiln type reactor for processing at a fluidizing zone, and a source of steam and a source of hydrogen connected to the fluidized bed reactor below the fluidizing zone. Optionally, a grinder can be provided in the kiln type reactor.

    摘要翻译： 一种用于将碳质材料转化为富含碳的气体流的方法和装置，包括在足以产生富含甲烷和一氧化碳的流的温度和压力下，使用氢气和蒸汽在加氢气化过程中加热含有碳质材料的浆料进料 该过程中的转换时间在5到45秒之间。 在具体实施方案中，含有碳质材料的浆料进料物料与氢气一起进料到窑式反应器中，然后送入流化床反应器。 提供了包括窑式反应器，连接到窑式反应器的输入端的浆料泵的装置，用于将氢源连接到窑式反应器的输入端的装置; 连接以接收在流化区处理的窑式反应器的输出的流化床反应器，以及连接到流化床下方的流化床反应器的蒸汽源和氢源。 任选地，可以在窑式反应器中提供研磨机。

    Appliance for converting household waste into energy
    8.
    发明申请
    Appliance for converting household waste into energy 有权
    将家庭垃圾转化为能源的设备

    公开(公告)号：US20070099039A1

    公开(公告)日：2007-05-03

    申请号：US11592093

    申请日：2006-11-02

    申请人： Terry Galloway

    发明人： Terry Galloway

    IPC分类号： H01M8/06 ,  A62D3/35

    CPC分类号： C10J3/005 ,  B09B3/00 ,  C10J3/20 ,  C10J2200/09 ,  C10J2300/0946 ,  C10J2300/0973 ,  C10J2300/1223 ,  C10J2300/123 ,  C10J2300/1646 ,  C10J2300/1671 ,  C10J2300/1823 ,  H01M8/04014 ,  H01M8/0631 ,  Y02E70/20 ,  Y02P20/129 ,  Y02W30/58

    摘要： A method and reactor system is configured as an appliance for the destruction of residential and building waste to form hydrogen-rich syngas. This syngas is used to power a fuel cell for the generation of electric power, steam and heat or cooling for use in residences and buildings as well as hydrogen fuel for vehicles. The waste conversion rector that carries out the endothermic reactions of steam reforming is heated with the waste heat and electrical power. Alternatively, this reactor can be heated by a natural gas burner. This reactor is designed as a rotary drum, into which are placed bags of waste that can consist of normal garbage as well as toilet solid waste. Glass and metal are not melted in this drum and are recovered as completely sterilized at the end of the process cycle.

    摘要翻译： 方法和反应器系统被配置为用于破坏住宅和建筑废物以形成富氢合成气的装置。 该合成气用于为燃料电池供电，用于产生用于住宅和建筑物中的电力，蒸汽和热量或冷却，以及用于车辆的氢燃料。 进行蒸汽重整的吸热反应的废物转化反应器用废热和电力加热。 或者，该反应器可以由天然气燃烧器加热。 该反应器设计为旋转鼓，其中放置可由正常垃圾和厕所固体废物组成的垃圾袋。 玻璃和金属在该滚筒中不熔化，并在加工周期结束时被完全消毒。

    Process and system for converting carbonaceous feedstocks into energy without greenhouse gas emissions
    9.
    发明授权
    Process and system for converting carbonaceous feedstocks into energy without greenhouse gas emissions 有权
    将碳质原料转化为没有温室气体排放的能源的过程和系统

    公开(公告)号：US07132183B2

    公开(公告)日：2006-11-07

    申请号：US10602536

    申请日：2003-06-23

    申请人： Terry R. Galloway

    发明人： Terry R. Galloway

    IPC分类号： H01M8/06

    CPC分类号： C10J3/24 ,  C10J3/005 ,  C10J3/10 ,  C10J2300/1246 ,  C10J2300/1612 ,  C10J2300/1646 ,  C10J2300/1659 ,  H01M8/0612 ,  H01M8/0668 ,  Y02E20/16 ,  Y02P30/10

    摘要： The process and system of the invention converts carbonaceous feedstock such as coal, hydrocarbon oil, natural gas, petroleum coke, oil shale, carbonaceous-containing waste oil, carbonaceous-containing medical waste, carbonaceous-containing hazardous waste, carbonaceous-containing medical waste, and mixtures thereof into electrical energy without the production of unwanted greenhouse emissions. The process and system uses a combination of a gasifier, e.g., a kiln, operating in the exit range of at least 700° to about 1600° C. (1300–2900° F.) to convert the carbonaceous feedstock and a greenhouse gas stream into a synthesis gas comprising mostly carbon monoxide and hydrogen without the need for expensive catalysts and or high pressure operations. One portion of the synthesis gas from the gasifier becomes electrochemically oxidized in an electricity-producing fuel cell into an exit gas comprising carbon dioxide and water. The latter is recycled back to the gasifier after a portion of water is condensed out. The second portion of the synthesis gas from the gasifier is converted into useful hydrocarbon products.

    摘要翻译： 本发明的方法和系统将碳，碳氢化合物油，天然气，石油焦，油页岩，含碳废油，含碳医疗废物，含碳危险废物，含碳化学医疗废物， 并将其混合物转化成电能，而不产生不需要的温室气体排放。 该方法和系统使用在至少700℃至约1600℃（1300-2900°F）的出口范围内操作的气化器（例如窑）的组合，以将碳质原料和温室气体流 成为主要包含一氧化碳和氢气的合成气体，而不需要昂贵的催化剂和/或高压操作。 来自气化器的一部分合成气在发电用燃料电池中电化学氧化成包含二氧化碳和水的出口气体。 一部分水冷凝后，后者再循环回气化炉。 来自气化器的合成气的第二部分转化为有用的烃产物。

    Thermal synthesis production of steel
    10.
    发明申请
    Thermal synthesis production of steel 有权
    热合成钢生产

    公开(公告)号：US20060196311A1

    公开(公告)日：2006-09-07

    申请号：US11070527

    申请日：2005-03-01

    申请人： Oren Peterson

    发明人： Oren Peterson

    IPC分类号： C21B13/08

    CPC分类号： C10J3/00 ,  C10J3/005 ,  C10J3/725 ,  C10J2200/09 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/16 ,  C10J2300/1606 ,  C10J2300/1609 ,  C21B13/0073 ,  C21B13/143 ,  C21B2100/22 ,  C21C1/02 ,  C21C5/562 ,  C21C5/567 ,  Y02P10/136 ,  Y02P10/216

    摘要： A process for producing liquid steel is disclosed. Carbon monoxide and oxygen may be combusted in a high temperature reactor. Iron and iron oxide materials, along with scrap steel if desired, may be placed in the high temperature reactor. Carbon dioxide produced in the high temperature reactor may be circulated through a back reactor vessel. Coke masses may be placed in the back reactor vessel. The coke may be formed by circulating heated carbon monoxide counter current to crushed coal in a rotary kiln. The carbon dioxide circulated through the back reactor vessel reacts with the coke to form carbon monoxide. The carbon monoxide may be conveyed to the high temperature reactor to be combusted with oxygen to produce the heat for forming the liquid steel.

    摘要翻译： 公开了一种生产液态钢的方法。 一氧化碳和氧气可能在高温反应器中燃烧。 如果需要，铁和氧化铁材料以及废钢可以放置在高温反应器中。 在高温反应器中产生的二氧化碳可以通过反向反应器容器循环。 焦炭质量可以放置在后反应器容器中。 可以通过在回转窑中将加热的一氧化碳逆流循环到粉碎煤上形成焦炭。 通过后反应器容器循环的二氧化碳与焦炭反应形成一氧化碳。 一氧化碳可以被输送到高温反应器中以与氧气一起燃烧以产生用于形成液态钢的热量。