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    METHODS, SYSTEMS, AND APPARATUSES FOR LOW-TEMPERATURE, FISCHER-TROPSCH WAX HYDROGENATION
    5.
    发明申请
    METHODS, SYSTEMS, AND APPARATUSES FOR LOW-TEMPERATURE, FISCHER-TROPSCH WAX HYDROGENATION 审中-公开
    FISCHER-TROPSCH WAX氢化方法，系统和装置

    公开(公告)号：US20160168486A1

    公开(公告)日：2016-06-16

    申请号：US14904122

    申请日：2014-08-21

    申请人： GI-GASIFICATION INTERNATIONAL (LUXEMBOURG), S.A.

    发明人： John HEMMINGS ,  Juan R. INGA

    IPC分类号： C10G45/00 ,  C10G67/02

    CPC分类号： C10G45/00 ,  B01J8/006 ,  B01J8/226 ,  B01J8/228 ,  B01J2208/00212 ,  B01J2208/0084 ,  B01J2208/00867 ,  B01J2208/025 ,  C10G2/33 ,  C10G45/02 ,  C10G45/16 ,  C10G45/22 ,  C10G45/58 ,  C10G45/66 ,  C10G47/04 ,  C10G47/26 ,  C10G67/02 ,  C10G2300/1022 ,  C10G2300/202 ,  C10G2300/4006

    摘要： A process for hydrogenating a Fischer-Tropsch (“FT”) wax includes placing hydrogenation catalyst particles within a low-temperature hydrogenation reactor having a mixing sub-system and a vent at the top for excess hydrogen, placing the FT wax at a low temperature up to a predetermined level within the low-temperature, hydrogenation reactor, leaving a vapor space above the predetermined level, adding hydrogen under a desired pressure into the low-temperature hydrogenation reactor, mixing the input FT wax, the hydrogen gas and the hydrogenating catalyst particles together to create a mixture using the mixing subsystem and continuing the mixing until the FT wax has hydrogenated, stopping the mixing to allow the hydrogenation catalyst particles to settle, and removing an hydrogenated FT wax with residual hydrogenating catalyst particles from the low-temperature hydrogenation reactor. The hydrogenated FT wax may be filtered and subjected to vacuum distillation. Other embodiments are also disclosed.

    摘要翻译： 用于氢化费 - 托（“FT”）蜡的方法包括将氢化催化剂颗粒放置在具有混合子系统的低温氢化反应器中并且在顶部具有用于过量氢气的通风口，将FT蜡置于低温 在低温氢化反应器中达到预定水平，留下高于预定水平的蒸气空间，将所需压力下的氢气加入到低温氢化反应器中，将输入的FT蜡，氢气和氢化催化剂混合 颗粒在一起以使用混合子系统产生混合物并继续混合直到FT蜡氢化，停止混合以使氢化催化剂颗粒沉降，并从低温氢化物除去具有残余氢化催化剂颗粒的氢化FT蜡 反应堆。 氢化FT蜡可以过滤并进行真空蒸馏。 还公开了其他实施例。

    Process for contacting one or more contaminated hydrocarbons
    6.
    发明授权
    Process for contacting one or more contaminated hydrocarbons 有权
    用于接触一种或多种被污染的烃的方法

    公开(公告)号：US09150470B2

    公开(公告)日：2015-10-06

    申请号：US13365210

    申请日：2012-02-02

    申请人： Mark Van Wees

    发明人： Mark Van Wees

    IPC分类号： C07C1/00 ,  C07C7/00 ,  C10G45/02 ,  C10G45/22

    CPC分类号： C07C7/00 ,  B01D1/065 ,  B01D1/22 ,  C10G45/02 ,  C10G45/22 ,  C10G2300/1077

    摘要： One exemplary embodiment can be a process. The process can include contacting one or more contaminated hydrocarbons with a hydrogen gas stream in a flash feed separator to generate a first liquid stream, stripping the first liquid stream to generate a residue stream, and separating the residue stream in a film generating evaporator to obtain a recovered distillate.

    摘要翻译： 一个示例性实施例可以是一个过程。 该方法可以包括使一种或多种被污染的烃与闪蒸进料分离器中的氢气流接触以产生第一液体流，汽提第一液流以产生残余物流，并将膜中产生的蒸发器中的残余物流分离，得到 回收的馏出物。

    Hydroprocessing light cycle oil in liquid-full reactors
    7.
    发明授权
    Hydroprocessing light cycle oil in liquid-full reactors 有权
    液体反应堆中的加氢轻循环油

    公开(公告)号：US09139783B2

    公开(公告)日：2015-09-22

    申请号：US14051495

    申请日：2013-10-11

    申请人： E I DU PONT DE NEMOURS AND COMPANY

    发明人： Hasan Dindi ,  Alan Howard Pulley ,  Thanh Gia Ta ,  Vincent Adam Kuperavage, Jr.

    IPC分类号： C10G57/00 ,  C10G65/12 ,  C10G45/22 ,  C10G7/00

    CPC分类号： C10G65/12 ,  C10G7/00 ,  C10G45/22 ,  C10G47/00 ,  C10G2300/1037 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/4081 ,  C10G2400/04

    摘要： A process for the hydroprocessing of a low-value light cycle oil (LCO) hydrocarbon feed to provide a high-value diesel-range product. The process comprises a hydrotreatment stage followed by a hydrocracking stage, each of which is conducted under liquid-full reaction conditions wherein substantially all the hydrogen supplied to the hydrotreating and hydrocracking reactions is dissolved in the liquid-phase hydrocarbon feed. Ammonia and optionally other gases formed during hydrotreatment are removed in a separation step prior to hydrocracking. The LCO feed is advantageously converted to diesel in high yield with little loss of hydrocarbon to naphtha.

    摘要翻译： 一种用于低价值轻循环油（LCO）烃进料加氢处理以提供高价值柴油范围产品的方法。 该方法包括加氢处理阶段，随后是加氢裂化阶段，每个步骤在液体完全反应条件下进行，其中供应到加氢处理和加氢裂化反应的基本上所有氢气都溶解在液相烃进料中。 在加氢处理之前，氨和任选的其它气体在分离步骤中被除去。 有利地，LCO进料以高产率转化为柴油，几乎没有烃与石脑油的损失。

    SYSTEM AND PROCESS FOR HYDROCRACKING AND HYDROGENATION
    10.
    发明申请
    SYSTEM AND PROCESS FOR HYDROCRACKING AND HYDROGENATION 审中-公开
    用于水力加氢和加氢的系统和方法

    公开(公告)号：US20140209509A1

    公开(公告)日：2014-07-31

    申请号：US13790693

    申请日：2013-03-08

    申请人： H R D CORPORATION

    发明人： Abbas Hassan ,  Aziz Hassan ,  Rayford G. Anthony ,  Gregory G. Borsinger

    IPC分类号： C10G45/00 ,  F17D1/00

    CPC分类号： C10G45/00 ,  B01F7/00766 ,  B01F13/1016 ,  B01J8/222 ,  B01J10/002 ,  B01J19/0066 ,  B01J19/1806 ,  B01J2219/0004 ,  B01J2219/00189 ,  C10G1/065 ,  C10G45/02 ,  C10G45/16 ,  C10G45/22 ,  C10G47/00 ,  C10G47/26 ,  C10G47/34 ,  C10G49/007 ,  Y10T137/0318

    摘要： Herein disclosed is a method for hydrogenation comprising: supersaturating a hydrocarbonaceous liquid or slurry stream in a high shear device with a gas stream comprising hydrogen and optionally one or more C1-C6 hydrocarbons to form a supersaturated dispersion; and introducing the supersaturated dispersion into a reactor in the presence of a hydrogenation catalyst to generate a product stream. In some embodiments, the catalyst is present as a slurry or a fluidized or fixed bed of catalyst. In some embodiments, the hydrogenation catalyst is mixed with the hydrocarbonaceous liquid or slurry stream and the gas stream in the high shear device. In some embodiments, the method further comprises recycling at least a portion of an off gas from the reactor, recycling at least a portion of the product stream from the reactor, or both. Also disclosed herein is a system for hydrogenation.

    摘要翻译： 本文公开了一种氢化方法，其包括：在高剪切装置中用含有氢气和任选的一种或多种C 1 -C 6烃的气流来过饱和烃类液体或浆料流以形成过饱和分散体; 并在加氢催化剂的存在下将过饱和分散体引入反应器中以产生产物流。 在一些实施方案中，催化剂作为浆料或催化剂的流化床或固定床存在。 在一些实施方案中，氢化催化剂与烃类液体或浆料流以及高剪切装置中的气流混合。 在一些实施方案中，该方法还包括将来自反应器的废气的至少一部分再循环至少一部分来自反应器的产物流或两者。 本文还公开了一种用于氢化的体系。