CATALYST ROLLER FOR GRAVITY-ASSISTED PARTICLE FLOW

    公开(公告)号:WO2018190988A8

    公开(公告)日:2018-10-18

    申请号:PCT/US2018/023075

    申请日:2018-03-19

    Abstract: Systems and methods are provided for controlling the flow and transport of catalyst particles within a reaction system. The flow of catalyst particles can be managed using a rotating disc or wheel that is configured within a roller volume to allow for control over the rate of catalyst flow while reducing or minimizing attrition of the catalyst particles. This can be achieved in part by maintaining a relationship between the center of the rotating disc, the inlet for catalyst particles to the roller volume, and the top wall of the roller volume so that catalyst particles are not exposed to compressive forces and/or abrasion during rotation of the disc. Additionally or alternately, the disc and roller volume surfaces can be configured to reduce or minimize the potential for catalyst particles to become trapped in "dead space" regions within the roller volume. By using a disc to provide force for transport of particles through the roller volume, the speed of catalyst movement can be controlled at relatively slow catalyst flow rates with a reduced or minimized risk for clogging or plugging within the roller volume.

    MERCAPTAN REMOVAL USING MICROEACTORS
    6.
    发明申请
    MERCAPTAN REMOVAL USING MICROEACTORS 审中-公开
    MERCAPTAN使用微生物去除

    公开(公告)号:WO2014099349A1

    公开(公告)日:2014-06-26

    申请号:PCT/US2013/072784

    申请日:2013-12-03

    Abstract: Processes are provided herein for producing naphtha boiling range products with a desired sulfur content by reducing the mercaptan content of the naphtha boiling range products after the products exit a hydroprocessing stage. Due to mercaptan reversion, naphtha boiling range products that contain even small amounts of olefins can have a higher than expected sulfur content after hydroprocessing. In order to reduce or mitigate the effects of mercaptan reversion, microchannel reactors (or microreactors) can be placed in a processing system downstream of a reactor that produces a low sulfur naphtha product. The microreactors can include a coating of metals that have activity for hydrodesulfurization. By passing at least a portion of the naphtha product through the downstream microreactors, the mercaptans formed by reversion reactions can be reduced or eliminated, resulting in a naphtha product with possessing a very low sulfur content.

    Abstract translation: 本文提供了通过在产物离开加氢处理阶段之后还原石脑油沸程产物的硫醇含量来生产具有所需硫含量的石脑油沸程产物的方法。 由于硫醇反转,含有甚至少量烯烃的石脑油沸程产品在加氢处理后可能具有高于预期的硫含量。 为了减少或减轻硫醇反转的影响,微通道反应器(或微反应器)可以放置在产生低硫石脑油产物的反应器下游的处理系统中。 微反应器可以包括具有加氢脱硫活性的金属涂层。 通过使至少一部分石脑油产物通过下游微反应器,可以减少或消除由反转反应形成的硫醇,导致具有非常低的硫含量的石脑油产品。

    ENHANCEMENT OF SATURATES CONTENT IN HEAVY HYDROCARBONS UTILIZING ULTRAFILTRATION
    7.
    发明申请
    ENHANCEMENT OF SATURATES CONTENT IN HEAVY HYDROCARBONS UTILIZING ULTRAFILTRATION 审中-公开
    通过超声波提高重油中的饱和度

    公开(公告)号:WO2009058227A1

    公开(公告)日:2009-05-07

    申请号:PCT/US2008/012133

    申请日:2008-10-24

    CPC classification number: C10G31/11 C10G2300/1033 C10G2300/107

    Abstract: This invention relates to an ultrafiltration process for separating a heavy hydrocarbon stream to produce an enriched saturates content stream(s) utilizing an ultrafiltration separations process. The enriched saturates content streams can then be further processed in refinery and petrochemical processes that will benefit from the higher content of saturated hydrocarbons produced from this separations process. The invention may be utilized to separate heavy hydrocarbon feedstreams, such as whole crudes, topped crudes, synthetic crude blends, shale oils, oils derived from bitumen, oils derived from tar sands, atmospheric resids, vacuum resids, or other heavy hydrocarbon streams into enriched saturates content product streams. The invention provides an economical method for separating heavy hydrocarbon stream components by molecular species instead of molecular boiling points.

    Abstract translation: 本发明涉及一种用于分离重质烃流以利用超滤分离方法产生富集的饱和物含量物流的超滤方法。 然后可以在炼油和石油化学方法中进一步处理富集的饱和物质流,这将从该分离过程产生的较高含量的饱和烃受益。 本发明可以用于分离重烃进料流,例如整个原油,顶部原油,合成粗混合物,页岩油,来自沥青的油,源自焦油砂的油,常压渣油,减压渣油或其它重质烃流进入富集 饱和内容产品流。 本发明提供了一种经分子物质代替分子沸点分离重质烃流成分的经济方法。

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