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    Fuel Composition
    96.
    发明申请
    Fuel Composition 有权
    燃料组成

    公开(公告)号：US20080229654A1

    公开(公告)日：2008-09-25

    申请号：US12065265

    申请日：2006-08-29

    Applicant: David Bradin

    Inventor： David Bradin

    IPC: C10L1/18

    CPC classification number: C11C3/006 ,  C10G2/32 ,  C10G3/00 ,  C10G3/50 ,  C10G47/00 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1022 ,  C10G2300/1025 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/14 ,  C10L1/1616 ,  C11C3/00 ,  C11C3/14 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678

    Abstract: Compositions and methods for forming hydrocarbon products from triglycerides are disclosed. In one aspect, the methods involve the thermal decomposition of fatty acids, which can be derived from the hydrolysis of triglycerides. The thermal decomposition products can be combined with low molecular weight olefins, such as Fischer-Tropsch synthesis products, and subjected to molecular averaging reactions. Alternatively, the products can be subjected to hydrocracking reactions, isomerization reactions, and the like. The products can be isolated in the gasoline, jet and/or diesel fuel ranges. Thus, vegetable oils and/or animal fats can be converted using water, catalysts, and heat, into conventional products in the gasoline, jet and/or diesel fuel ranges. These products are virtually indistinguishable from those derived from their petroleum-based analogs, except that they can have virtually no aromatic, sulfur or nitrogen content, they are derived, in whole or in part, from renewable resources, and can also be derived from domestically available coal and/or natural gas.

    Abstract translation: 公开了从甘油三酯形成烃产物的组合物和方法。 在一个方面，所述方法涉及脂肪酸的热分解，其可以源于甘油三酸酯的水解。 热分解产物可与低分子量烯烃如费 - 托合成产物结合，并进行分子平均反应。 或者，产物可以进行加氢裂化反应，异构化反应等。 产品可以在汽油，喷气和/或柴油燃料范围内分离。 因此，植物油和/或动物脂肪可以使用水，催化剂和热量转化成汽油，喷气和/或柴油燃料范围内的常规产品。 这些产品几乎与来自其石油类似物的产品几乎无法区分，除了它们几乎不具有芳香族，硫或氮的含量，它们全部或部分来自可再生资源，也可以从国内得到 可用的煤和/或天然气。

    Process For Converting Difficultly Convertible Oxygenates to Gasoline
    97.
    发明申请
    Process For Converting Difficultly Convertible Oxygenates to Gasoline 有权
    将可转换的可转换氧化物转化为汽油的方法

    公开(公告)号：US20080228021A1

    公开(公告)日：2008-09-18

    申请号：US12063021

    申请日：2006-08-16

    Applicant: Finn Joensen ,  Bodil Voss ,  Jesper Nerlov

    Inventor： Finn Joensen ,  Bodil Voss ,  Jesper Nerlov

    IPC: C07C1/00

    CPC classification number: C07C29/151 ,  C10G3/00 ,  C10G3/49 ,  C10G2300/1022 ,  C10G2300/4081 ,  C10G2400/02 ,  C10L1/06 ,  Y02P30/20 ,  C07C31/04

    Abstract: Process for converting oxygenate compounds to hydrocarbons comprising the steps: (a) introducing a feed stream of synthesis gas to a synthesis section for the production of easily convertible oxygenates, (b) passing the effluent stream from said synthesis section containing easily convertible oxygenates to a gasoline synthesis section, (c) passing the effluent of said gasoline synthesis section to a separator and withdrawing from said separator hydrocarbons boiling in the gasoline boiling range, (d) admixing a recycle stream from the separator containing unconverted synthesis gas volatile hydrocarbons with the feed stream of synthesis gas of step (a), (e) introducing a feed containing difficulty convertible oxygenates to the synthesis section of step (a).

    Abstract translation: 将含氧化合物转化为烃的方法，包括以下步骤：（a）将合成气的进料流引入合成段，以生产容易转化的含氧化合物，（b）将含有易转化含氧化合物的合成段的流出物流送至 汽油合成段，（c）将所述汽油合成段的流出物通入分离器并从汽油沸程沸腾的所述分离器中取出，（d）将含有未转化的合成气挥发性烃的分离器的再循环流与进料混合 步骤（a）的合成气流，（e）将含有难以转化的含氧化合物的进料引入步骤（a）的合成部分。

    Process for converting gaseous alkanes to liquid hydrocarbons
    100.
    发明申请
    Process for converting gaseous alkanes to liquid hydrocarbons 有权
    将气态烷烃转化为液态烃的方法

    公开(公告)号：US20050234277A1

    公开(公告)日：2005-10-20

    申请号：US11101886

    申请日：2005-04-08

    Applicant: John Waycuilis

    Inventor： John Waycuilis

    IPC: C01B7/09 ,  C07C1/00 ,  C07C1/26 ,  C07C2/00 ,  C07C17/10 ,  C10G3/00

    CPC classification number: C01B9/04 ,  C01B7/093 ,  C01B7/096 ,  C07C1/26 ,  C07C17/10 ,  C07C2529/40 ,  C10G3/00 ,  C10G2300/1025 ,  Y02P30/20 ,  C07C19/075

    Abstract: A process for converting gaseous alkanes to liquid hydrocarbons wherein a gaseous feed containing alkanes is reacted with a dry bromine vapor to form alkyl bromides and hydrobromic acid vapor. The mixture of alkyl bromides and hydrobromic acid are then reacted over a synthetic crystalline alumino-silicate catalyst, such as a ZSM-5 zeolite, at a temperature of from about 150° C. to about 450° C. so as to form higher molecular weight hydrocarbons and hydrobromic acid vapor. Propane and butane which comprise a portion of the products may be recovered or recycled back through the process to form additional C5+ hydrocarbons. Various methods are disclosed to remove the hydrobromic acid vapor from the higher molecular weight hydrocarbons and to generate bromine from the hydrobromic acid for use in the process.

    Abstract translation: 将气态烷烃转化为液态烃的方法，其中含有烷烃的气态原料与干溴蒸气反应形成烷基溴和氢溴酸蒸气。 然后将烷基溴和氢溴酸的混合物在约150℃至约450℃的温度下在合成的结晶铝硅酸盐催化剂如ZSM-5沸石上反应，以形成更高分子量 碳氢化合物和氢溴酸蒸气。 包含产物的一部分的丙烷和丁烷可以通过该方法回收或循环回来以形成另外的C 5+烃。 公开了各种方法以从较高分子量烃中除去氢溴酸蒸气，并从该氢过溴产生溴用于该方法。

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