Hydrogen use in a GTL plant
    2.
    发明申请
    Hydrogen use in a GTL plant 失效
    氢气用于GTL工厂

    公开(公告)号:US20040180974A1

    公开(公告)日:2004-09-16

    申请号:US10388905

    申请日:2003-03-15

    Abstract: The present invention provides a process for managing hydrogen in a hydrocarbon gas to liquid plant. The process includes passing a syngas feed stream produced by a partial oxidation reactor to a Fischer-Tropsch reactor, thereby converting the syngas to hydrocarbon liquids. The hydrogen management process further includes passing a second hydrogen rich stream produced by an auxiliary source to a hydrogen user such as an FT water stripper, an FT catalyst regeneration unit, and an FT product upgrading unit. The auxiliary source could be a process for converting hydrocarbons to syngas, a process for converting hydrocarbons to olefins, a process for converting hydrocarbons to aromatics, a process for catalytically dehydrogenating hydrocarbons, a process for catalytically cracking hydrocarbons, a process for refining petroleum, and a process for converting hydrocarbons to carbon filaments.

    Abstract translation: 本发明提供了一种管理烃气体中的氢气到液态装置的方法。 该方法包括将由部分氧化反应器产生的合成气进料流送至费 - 托反应器,从而将合成气转化成烃液体。 氢管理方法还包括将由辅助源产生的第二富氢流通过诸如FT水汽提塔,FT催化剂再生单元和FT产物升级单元之类的氢用户。 辅助源可以是将烃转化为合成气的方法,将烃转化为烯烃的方法,将烃转化为芳族化合物的方法,烃的催化脱氢方法,烃催化裂解方法,精炼石油的方法和 将烃转化为碳丝的方法。

    High hydrothermal stability catalyst support
    6.
    发明申请
    High hydrothermal stability catalyst support 审中-公开
    高水热稳定催化剂支持

    公开(公告)号:US20040127352A1

    公开(公告)日:2004-07-01

    申请号:US10687017

    申请日:2003-10-16

    Abstract: Methods are disclosed for preparing hydrothermally-stable structurally-promoted refractory-oxide catalyst supports, which includes mixing precursors of the refractory oxide and of at least one structural promoter and calcining the mixture. The methods feature the incorporation of at least one structural promoter into the lattice of a refractory-oxide material such as alumina. The hydrothermally-stable structurally-promoted refractory-oxide catalyst supports are useful in hydrothermal catalytic processes such as Fischer-Tropsch reactions.

    Abstract translation: 公开了用于制备水热稳定的结构促进的耐火氧化物催化剂载体的方法,其包括混合难熔氧化物的前体和至少一种结构促进剂并煅烧该混合物。 该方法的特征在于将至少一种结构促进剂掺入耐火氧化物材料如氧化铝的晶格中。 水热稳定的结构促进耐火氧化物催化剂载体可用于水热催化方法如费 - 托反应。

    Optimized solid/liquid separation system for multiphase converters
    7.
    发明申请
    Optimized solid/liquid separation system for multiphase converters 失效
    用于多相转换器的优化固/液分离系统

    公开(公告)号:US20030232894A1

    公开(公告)日:2003-12-18

    申请号:US10417307

    申请日:2003-04-16

    CPC classification number: B01D37/02 B01D29/15 B01D29/60 B01D37/043

    Abstract: Methods for producing clean liquid/wax products from a slurry used in a Fischer-Tropsch reactor are disclosed. In general, one embodiment of the present invention comprises a solid/liquid filtration system having a filter medium comprising a substrate and a filter cake deposited on the substrate, wherein the filter cake is generated by deposition of solids from the slurry. The thickness of the filter cake can be maintained within a desired range by controlling the slurry velocity and/or the pressure differential across the filter medium. This invention relates to a method of operation of such filtration system which increases filtration cycle time and improved filtrate quality resulting in very low solid content in filtrate.

    Abstract translation: 公开了从费 - 托反应器中使用的浆料制备清洁液体/蜡产品的方法。 通常,本发明的一个实施方案包括具有过滤介质的固体/液体过滤系统,该过滤介质包括沉积在基底上的基底和滤饼,其中通过从浆液沉积固体产生滤饼。 通过控制过滤介质上的浆料速度和/或压力差,滤饼的厚度可以保持在所需范围内。 本发明涉及这种过滤系统的操作方法,其增加了过滤循环时间并提高了滤液质量,导致滤液中固体含量非常低。

    Octane improvement of a hydrocarbon stream
    8.
    发明申请
    Octane improvement of a hydrocarbon stream 有权
    辛烷值改善烃流

    公开(公告)号:US20040236164A1

    公开(公告)日:2004-11-25

    申请号:US10795895

    申请日:2004-03-08

    CPC classification number: C10G59/00

    Abstract: The invention relates to methods for improving the octane number of a synthetic naphtha stream and optionally for producing olefins and/or solvents. In one embodiment, the method comprises aromatizing at least a portion of a synthetic naphtha stream to produce an aromatized hydrocarbon stream; and isomerizing at least a portion of the aromatized hydrocarbon stream to produce an isomerized aromatized hydrocarbon stream having a higher octane rating than the synthetic naphtha stream. Alternatively, the method comprises providing at least three synthetic naphtha cuts comprising a C4-C5 stream; a C6-C8 stream and a C9-C11 stream; aromatizing some of the C6-C8 stream to form an aromatized hydrocarbon stream with a higher octane number; steam cracking some of the C6-C8 stream and optionally the C9-C11 stream to form olefins; and selling some portions of C9-C11 stream as solvents. In preferred embodiments, the synthetic naphtha is derived from Fischer-Tropsch synthesis.

    Abstract translation: 本发明涉及用于改进合成石脑油流的辛烷值并任选地用于生产烯烃和/或溶剂的方法。 在一个实施方案中,该方法包括将至少一部分合成石脑油流芳构化以产生芳族烃流; 并使至少一部分芳构化烃物流异构化以产生具有比合成石脑油流更高辛烷值的异构化芳构化烃物流。 或者,该方法包括提供包含C4-C5流的至少三个合成石脑油切割; C6-C8流和C9-C11流; 使一些C 6 -C 8流芳构化以形成具有较高辛烷值的芳构化烃流; 蒸汽裂解一些C6-C8流和任选的C9-C11流以形成烯烃; 并将C9-C11流的一些部分作为溶剂出售。 在优选的实施方案中,合成石脑油衍生自费 - 托合成。

    Method for reducing the maximum water concentration in a multi-phase column reactor

    公开(公告)号:US20040204508A1

    公开(公告)日:2004-10-14

    申请号:US10834152

    申请日:2004-04-28

    CPC classification number: C10G2/342 B01F13/0255 B01J8/22

    Abstract: The present invention relates to a method and apparatus for reducing the maximum water concentration in multi-phase reactors operating at Fischer-Tropsch conditions. In a preferred embodiment of the present invention, a method of reducing the maximum concentration of water in a multi-phase reactor containing an expanded slurry bed and a water-rich slurry region for Fisher-Tropsch synthesis includes changing the flow structure of a predetermined region in the reactor. The flow structure may be changed by introducing a mixing enhancing fluid into the predetermined region, installing baffles into the predetermined region, or by other methods known in the art. Preferably the predetermined region is located between null H and H and between null R and R, where H is the height of the expanded slurry bed and R is the radius of the reactor.

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