Fuel cell system
    61.
    发明申请
    Fuel cell system 审中-公开
    燃料电池系统

    公开(公告)号:US20060172174A1

    公开(公告)日:2006-08-03

    申请号:US11366696

    申请日:2006-03-01

    Inventor: In Son Dong Suh Ju Kim

    Abstract: A fuel cell system including a stack provided with a plurality of unit cells generating electricity based on a chemical reaction between hydrogen gas and oxygen gas, and a reformer for supplying the hydrogen gas obtained by reforming hydrogen-containing fuel to the stack. A fuel storage tank is provided for storing the hydrogen-containing fuel to be supplied to the reformer and an air supplier is provided for supplying air to the stack. An injection nozzle assembly is detachably provided and includes an injection means placed in front of the inlet formed in the first side of the reformer to introduce the hydrogen-containing fuel from the fuel storage tank.

    Abstract translation: 一种燃料电池系统,包括具有基于氢气和氧气之间的化学反应发电的多个单电池的堆叠体,以及用于将通过将含氢燃料重整而获得的氢气供给到所述堆的重整器。 提供一种燃料储罐,用于储存供应给重整器的含氢燃料,并且提供空气供应器用于将空气供给到堆。 注射喷嘴组件可拆卸地设置,并且包括设置在重整器第一侧的入口前方的喷射装置,以将来自燃料储罐的含氢燃料引入。

    Flow control in a three-phase monolithic catalyst reactor
    67.
    发明授权
    Flow control in a three-phase monolithic catalyst reactor 失效
    三相整体式催化剂反应器中的流量控制

    公开(公告)号:US06822128B2

    公开(公告)日:2004-11-23

    申请号:US10027645

    申请日:2001-12-20

    Abstract: A method is disclosed for maintaining a volumetric gas to liquid ratio in a segmented gas/liquid flow along a reactor of monolithic catalyst beds in series. The present invention includes the steps of: initiating the segmented gas/liquid flow at a first end of the reactor by introducing feed liquid and feed gas both at a predetermined volume and a predetermined flow rate; injecting an additional amount of gas at least once into any of the spaces between catalyst beds; and combining the segments of the segmented gas/liquid flow at a second end of the reactor. The injection of gas is controlled such that the segmented gas/liquid flow can be maintained near or at the Taylor regime.

    Abstract translation: 公开了一种用于在沿着整体式催化剂床的反应器串联的分段气/液流中维持体积气体与液体比的方法。 本发明包括以下步骤:通过以预定的体积和预定流量引入进料液体和进料气体来在反应器的第一端引发分段的气/液流; 将至少一次额外量的气体注入催化剂床之间的任何空间; 并且在反应器的第二端处组合分段的气体/液体流的段。 控制气体的注入使得分段的气体/液体流可以保持在泰勒状态附近或处于泰勒状态。

    Production of gaseous chloramine
    68.
    发明申请
    Production of gaseous chloramine 失效
    生产气态氯胺

    公开(公告)号:US20040141905A1

    公开(公告)日:2004-07-22

    申请号:US10713996

    申请日:2003-11-14

    Abstract: The present invention provides a reactor for the gas-phase reaction of commercially available gases in the presence of an inert carrier gas to form product gas. The reactor has a streamlined, compact configuration and at least one solids collection and removal system downstream of the reactor, where solids are efficiently removed from the product gas stream, leaving high purity product gas. The removal system allows for a simple reactor design, which is easy to clean and operates continuously over longer periods of time.

    Abstract translation: 本发明提供了一种用于在惰性载气存在下商业上可获得的气体进行气相反应以形成产物气体的反应器。 反应器具有流线型,紧凑的构造和在反应器下游的至少一个固体收集和去除系统,其中固体从产物气流中有效地除去,留下高纯度产物气体。 拆卸系统允许简单的反应器设计,其易于清洁并且在更长的时间段内连续操作。

    Deep conversion combining the demetallization and the conversion of crudes, residues or heavy oils into light liquids with pure or impure oxygenated compounds
    70.
    发明申请
    Deep conversion combining the demetallization and the conversion of crudes, residues or heavy oils into light liquids with pure or impure oxygenated compounds 失效
    深层转换将原油,残渣或重油转化为纯化或不纯氧化化合物的轻质液体脱金属

    公开(公告)号:US20040065589A1

    公开(公告)日:2004-04-08

    申请号:US10428212

    申请日:2003-05-02

    Inventor: Pierre Jorgensen

    Abstract: A process for the conversion of hydrocarbons that are solid or have a high boiling temperature and may be laden with metals, sulfur or sediments, into liquids (gasolines, gas oil, fuels) with the help of a jet of gas properly superheated between 600 and 800null C. The process comprises preheating a feed 5 in a heater 8 to a temperature below the selected temperature of a reactor 10. This feed is injected by injectors 4 into the empty reactor 10 (i.e., without catalyst.) The feed is treated with a jet of gas or superheated steam from superheater 2 to activate the feed. The activated products in the feed are allowed to stabilize at the selected temperature and at a selected pressure in the reactor and are then run through a series of extractors 13 to separate heavy and light hydrocarbons and to demetallize the feed. Useful products appearing in the form of water/hydrocarbon emulsions are generally demulsified in emulsion breaker 16 to form water laden with different impurities. The light phase containing the final hydrocarbons is heated in heater 98 and is separated into cuts of conventional products, according to the demand for refining by an extractor 18 similar to 13.

    Abstract translation: 一种将固体或具有高沸点温度的烃转化成金属,硫或沉淀物的烃转化为液体(汽油,瓦斯油,燃料)的方法,借助于600〜 该方法包括将加热器8中的进料5预热到低于反应器10的选定温度的温度。该进料通过喷射器4注入空反应器10(即,不含催化剂)。进料被处理 用过热器2的气体喷射或过热蒸汽激活进料。 允许进料中的活化产物在反应器中选定的温度和选择的压力下稳定,然后通过一系列萃取器13分离重质烃和轻质烃并使进料脱金属。 以水/烃乳液形式出现的有用产品通常在破乳剂16中破乳以形成含有不同杂质的水。 含有最终碳氢化合物的轻相在加热器98中加热,并根据类似于13的萃取器18的精炼需求分离成常规产品的切割。

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