Process for Removing Color Bodies from Hydrocarbon-Based Fuels Using Activated Carbons
    73.
    发明申请
    Process for Removing Color Bodies from Hydrocarbon-Based Fuels Using Activated Carbons 审中-公开
    使用活性炭从烃类燃料中去除色体的方法

    公开(公告)号:US20060219599A1

    公开(公告)日:2006-10-05

    申请号:US11277798

    申请日:2006-03-29

    Abstract: A process for removing color bodies from hydrocarbon-based fuels, particularly gasoline, using an activated carbon is disclosed. Color bodies are removed from the fuel by contacting the fuel with such activated carbon having within this pore structure a fuel decolorizing amount of polymerized phosphoric acid or reduced transition metals. Phosphoric acid may be added to a non-phosphoric acid-activated carbon (such as steam activated coal-based) prior to the subsequent heat treatment or one can take advantage of residual phosphoric acid present in, for example, a phosphoric acid-activated wood-based carbon. Similarly, transition metals such as copper may be added to an activated carbon in a salt form in addition to whatever is already present therein as impurities.

    Abstract translation: 公开了一种使用活性炭从碳氢化合物燃料,特别是汽油中除去色体的方法。 通过使燃料与在该孔结构内具有燃料脱色量的聚合磷酸或还原的过渡金属的活性炭接触来将燃料从燃料中除去。 在随后的热处理之前,可以将磷酸加入到非磷酸活性炭(例如蒸汽活化的煤基)中,或者可以利用存在于例如磷酸活化的木材中的残留磷酸 的碳。 类似地,除了作为杂质存在的任何物质之外,过渡金属如铜可以以盐形式加入到活性炭中。

    Deep conversion combining the demetallization and the conversion of crudes, residues or heavy oils into light liquids with pure or impure oxygenated compounds
    75.
    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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