SYSTEM AND PROCESS FOR WATER TREATMENT
    112.
    发明申请
    SYSTEM AND PROCESS FOR WATER TREATMENT 审中-公开
    水处理系统和工艺

    公开(公告)号:WO2009003022A1

    公开(公告)日:2008-12-31

    申请号:PCT/US2008/068161

    申请日:2008-06-25

    Abstract: A method for removing contaminant from feedwater by forming a dispersion comprising bubbles of a treatment gas in a continuous phase comprising feedwater, wherein the bubbles have a mean diameter of less than about 5 microns and wherein the treatment gas is selected from air, oxygen, and chlorine. A method for removing contaminants from a feedwater by subjecting a fluid mixture comprising feedwater and a treatment gas to a shear rate greater than 20,000 s-1 in a high shear device to produce a dispersion of treatment gas in a continuous phase of the feedwater. A system for treating feedwater to remove contaminants therefrom is also presented, the system comprising at least one high shear mixing device comprising at least one generator comprising a rotor and a stator separated by a shear gap; and a pump configured for delivering feedwater and treatment gas to the high shear mixing device.

    Abstract translation: 一种通过在包括给水的连续相中形成包含处理气体气泡的分散体来除去给水中的污染物的方法,其中气泡的平均直径小于约5微米,其中处理气体选自空气,氧气和 氯。 一种通过在高剪切装置中使包含给水和处理气体的流体混合物的剪切速率大于20,000s -1的流体混合物从给水中除去污染物的方法,以在给水的连续相中产生处理气体的分散体。 还提供了一种用于处理给水以除去污染物的系统,该系统包括至少一个高剪切混合装置,其包括至少一个包括转子和由剪切间隔分隔的定子的发生器; 以及构造成用于将给水和处理气体输送到高剪切混合装置的泵。

    SYSTEM AND PROCESS FOR THERMAL CRACKING AND STEAM CRACKING
    117.
    发明申请
    SYSTEM AND PROCESS FOR THERMAL CRACKING AND STEAM CRACKING 审中-公开
    热裂解和蒸汽破碎的系统和方法

    公开(公告)号:WO2014116271A1

    公开(公告)日:2014-07-31

    申请号:PCT/US2013/029828

    申请日:2013-03-08

    Abstract: Herein disclosed is a method for thermal cracking or steam cracking of hydrocarbons comprising: supersaturating a hydrocarbonaceous liquid or slurry stream in a high shear device with a gas stream comprising steam or hydrogen and optionally one or more C1-C6 hydrocarbons to form a supersaturated dispersion; and introducing the supersaturated dispersion into a thermal cracking or steam cracking reactor to generate a product stream. In some embodiments, the method further comprises contacting the supersaturated dispersion with a cracking catalyst in a slurry, a fluidized catalyst bed, or a fixed catalyst bed. In some embodiments, the cracking catalyst is mixed with the hydrocarbonaceous liquid or slurry stream and the gas stream in the high shear device. Herein also disclosed is a system for thermal cracking or steam cracking of hydrocarbons.

    Abstract translation: 本文公开了一种用于烃的热裂化或蒸汽裂化的方法,其包括:在高剪切装置中用含有蒸汽或氢气的气流和任选的一种或多种C 1 -C 6烃过饱和含烃液体或浆料流以形成过饱和分散体; 并将过饱和分散体引入热裂解或蒸汽裂解反应器中以产生产物流。 在一些实施方案中,该方法还包括使过饱和分散体与浆料,流化催化剂床或固定催化剂床中的裂化催化剂接触。 在一些实施方案中,裂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。 本文还公开了一种用于烃的热裂解或蒸汽裂化的系统。

    HIGH SHEAR APPLICATION IN PROCESSING OILS
    118.
    发明申请
    HIGH SHEAR APPLICATION IN PROCESSING OILS 审中-公开
    加工油中的高剪切应用

    公开(公告)号:WO2013151652A1

    公开(公告)日:2013-10-10

    申请号:PCT/US2013/029423

    申请日:2013-03-06

    Abstract: Herein disclosed is a method of processing oil, comprising providing a high shear device comprising at least one rotor and at least one complementarily-shaped stator configured to mix a gas with a liquid; contacting a gas with an oil in the high shear device, wherein the gas is an inert gas or a reactive gas; and forming a product, wherein the product is a solution, a dispersion, or combination thereof. Herein also disclosed is a high shear system for processing oil, comprising; at least one high shear device, having an inlet and at least one rotor and at least one complementarily-shaped stator configured to mix a gas with a liquid; a gas source fluidly connected to the inlet; an oil source fluidly connected to the inlet; and a pump positioned upstream of a high shear device, the pump in fluid connection with the inlet and the oil source.

    Abstract translation: 本文公开了一种处理油的方法,包括提供高剪切装置,其包括至少一个转子和构造成将气体与液体混合的至少一个互补形定子; 在高剪切装置中使气体与油接触,其中气体是惰性气体或反应气体; 并形成产品,其中产物是溶液,分散体或其组合。 本文还公开了一种用于加工油的高剪切系统,其包括: 至少一个高剪切装置,具有入口和至少一个转子以及构造成将气体与液体混合的至少一个互补形状的定子; 与入口流体连接的气体源; 与入口流体连接的油源; 以及位于高剪切装置上游的泵,该泵与入口和油源流体连接。

    CRUDE OIL DESULFURIZATION
    119.
    发明申请
    CRUDE OIL DESULFURIZATION 审中-公开
    原油脱硫

    公开(公告)号:WO2012021358A2

    公开(公告)日:2012-02-16

    申请号:PCT/US2011/046476

    申请日:2011-08-03

    Abstract: A method of removing sulfur from sour oil by subjecting sour oil having a first sulfur content to high shear in the presence of at least one desulfurizing agent to produce a high shear treated stream, wherein the at least one desulfurizing agent is selected from the group consisting of bases and inorganic salts, and separating both a sulfur-rich product and a sweetened oil product from the high shear-treated stream, wherein the sulfur-rich product comprises elemental sulfur and wherein the sweetened oil product has a second sulfur content that is less than the first sulfur content. A system for reducing the sulfur content of sour oil via at least one high shear device comprising at least one rotor and at least one complementarily-shaped stator, and at least one separation device configured to separate a sulfur-rich product and sweetened oil from the high shear-treated stream.

    Abstract translation: 一种通过在至少一种脱硫剂的存在下使具有第一硫含量的酸油高剪切以产生高剪切处理的流来从酸性油中除去硫的方法,其中所述至少一种脱硫剂选自 的碱和无机盐,并且从高剪切处理的流中分离富硫产物和甜油产物,其中富硫产物包含元素硫,并且其中甜化油产物具有较少的第二硫含量 比第一硫含量高。 一种用于通过至少一个包括至少一个转子和至少一个互补形状的定子的高剪切装置降低酸性油的硫含量的系统,以及至少一个分离装置,其被配置成将富硫产物和甜油从 高剪切处理的流。

    METHOD OF MAKING ALKYLENE GLYCOLS
    120.
    发明申请
    METHOD OF MAKING ALKYLENE GLYCOLS 审中-公开
    制备亚苄基甘露糖的方法

    公开(公告)号:WO2011162837A1

    公开(公告)日:2011-12-29

    申请号:PCT/US2011/026719

    申请日:2011-03-01

    Abstract: Herein disclosed is a method of hydrating an alkylene oxide. In an embodiment, the method comprises (a) forming a first stream comprising an alkylene oxide and water; (b) flowing the first stream through a high shear device to produce a second stream; and (c) recovering an alkylene glycol from the second stream. In some embodiments, the method further comprises contacting the second stream with a catalyst in a reactor to hydrate the alkylene oxide and form the alkylene glycol. In some embodiments, alkylene oxide comprises ethylene oxide, propylene oxide, butylene oxide, or combinations thereof. In some embodiments, producing the second stream comprises an energy expenditure of at least about 1000 W/m3. In some embodiments, the catalyst comprises an amine, an acid catalyst, an organometallic compound, an alkali metal halide, a quaternary ammonium halide, a zeolite, or combinations thereof. In some embodiments, the alkylene glycol comprises ethylene glycol.

    Abstract translation: 本文公开了一种使烯化氧水合的方法。 在一个实施方案中,该方法包括(a)形成包含环氧烷和水的第一物流; (b)使第一流通过高剪切装置流动以产生第二流; 和(c)从第二料流中回收亚烷基二醇。 在一些实施方案中,该方法还包括使第二料流与反应器中的催化剂接触以水合烯化氧并形成亚烷基二醇。 在一些实施方案中,环氧烷包括环氧乙烷,环氧丙烷,环氧丁烷或其组合。 在一些实施方案中,生产第二流包含至少约1000W / m 3的能量消耗。 在一些实施方案中,催化剂包含胺,酸催化剂,有机金属化合物,碱金属卤化物,季铵卤化物,沸石或其组合。 在一些实施方案中,亚烷基二醇包括乙二醇。

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