PROCESS FOR REMOVING POLAR COMPONENTS FROM A PROCESS STREAM TO PREVENT HEAT LOSS
    15.
    发明申请
    PROCESS FOR REMOVING POLAR COMPONENTS FROM A PROCESS STREAM TO PREVENT HEAT LOSS 有权
    从流程流中移除极性组件以防止热损失的过程

    公开(公告)号:US20100037773A1

    公开(公告)日:2010-02-18

    申请号:US12537277

    申请日:2009-08-07

    Abstract: A process and system for removing polar components from a process stream in a refinery process without cooling the process stream are disclosed. The process stream is fed to a first adsorber unit to remove contaminants containing sulfur from the process stream. The process stream is processed within the first adsorber unit to remove sulfur containing contaminants. The process stream is processed with the first adsorber unit at substantially the same elevated temperature. The process stream is processed within the first adsorber unit by exposing the process stream to at least one of a metal oxide and a mixed metal oxide to remove the sulfur containing contaminants from the process stream and produce a metal sulfide and a desulfurized process stream. The metal sulfide may be exposed to a stream of oxygen to regenerate the at least one of a metal oxide and a mixed metal oxide. The desulfurized process stream may be exposed to at least one of the regenerated metal oxide and regenerated mixed metal oxide to remove moisture from the desulfurized process stream. The desulfurized process stream is then fed through a second adsorber unit to remove contaminants containing nitrogen from the process stream. The process stream is processed within the second adsorber unit to remove nitrogen containing contaminants, where the process stream being processed at substantially the same elevated temperature. The process stream is processed within the second adsorber unit by exposing the process stream to at least one of a molecular sieve and zeolites to remove nitrogen containing contaminants from the process stream.

    Abstract translation: 公开了一种用于在炼油工艺中从工艺流中除去极性组分而不冷却工艺流的方法和系统。 将工艺流送入第一吸附器单元以从工艺流中除去含有硫的污染物。 在第一吸附器单元内处理工艺流以除去含硫污染物。 在基本上相同的高温下用第一吸附器单元处理工艺流。 通过将工艺流暴露于金属氧化物和混合金属氧化物中的至少一种以从工艺流中除去含硫污染物并生产金属硫化物和脱硫工艺流,在第一吸附器单元内处理工艺流。 金属硫化物可以暴露于氧气流中以再生金属氧化物和混合金属氧化物中的至少一种。 脱硫工艺物流可以暴露于再生金属氧化物和再生混合金属氧化物中的至少一种,以从脱硫工艺物流中除去水分。 然后将脱硫的工艺物流通过第二吸附器单元以从工艺流中除去含有氮的污染物。 在第二吸附器单元内处理工艺流以除去含氮污染物,其中工艺流在基本相同的高温下进行处理。 通过将工艺流暴露于分子筛和沸石中的至少一种以从工艺流中除去含氮污染物,在第二吸附器单元内处理工艺流。

    Process for upgrading whole crude oil to remove nitrogen and sulfur compounds
    17.
    发明申请
    Process for upgrading whole crude oil to remove nitrogen and sulfur compounds 有权
    整个原油升级除氮和硫化合物的工艺

    公开(公告)号:US20090120842A1

    公开(公告)日:2009-05-14

    申请号:US11985533

    申请日:2007-11-14

    Abstract: A crude oil feedstream is treated to remove or reduce the content of known undesired heteroatomic and polynuclear aromatic compounds containing nitrogen and sulfur by contacting the feedstream with one or more solid adsorbent materials selected from attapulgus clay, alumina, silica gel and activated carbon in a mixing vessel for a time that is sufficient to optimize the adsorption of the undesired compounds from the crude oil, subjecting the mixture to atmospheric flash distillation and then to vacuum flash distillation to recover presorbed boiling ranges of products having a lowered content of the undesired compounds, and preferably regenerating at least a portion of the solid adsorbent material for reuse in the process.

    Abstract translation: 处理原油进料流以除去或减少含有氮和硫的已知不需要的杂原子和多核芳族化合物的含量,其通过将进料流与选自attapulgus粘土,氧化铝,硅胶和活性炭的一种或多种固体吸附材料接触,混合 容器足以优化来自原油的不期望的化合物的吸附,使混合物经历大气闪蒸,然后进行真空闪蒸以回收具有降低的不期望的化合物含量的产物的沸点范围,以及 优选地在该过程中再生至少一部分固体吸附剂材料以供再利用。

    Process for desulphurizing gasoline by converting sulphur-containing compounds to higher boiling point compounds
    18.
    发明授权
    Process for desulphurizing gasoline by converting sulphur-containing compounds to higher boiling point compounds 有权
    通过将含硫化合物转化为高沸点化合物来脱硫汽油的方法

    公开(公告)号:US07504022B2

    公开(公告)日:2009-03-17

    申请号:US11405676

    申请日:2006-04-18

    Applicant: Florent Picard

    Inventor: Florent Picard

    CPC classification number: C10G17/095 C10G25/05

    Abstract: A process for desulphurizing a gasoline cut containing olefins, sulphur-containing compounds and optionally molecules belonging to C3 and C4 cuts comprises at least a first step A for contacting said gasoline cut with an acidic resin having an acid capacity of more than 4.7 equivalents per kg and a specific surface area of less than 55 m2/g, and a second step B for fractionation of the mixture from the first step.

    Abstract translation: 含有烯烃,含硫化合物和任选地分别属于C3和C4馏分的汽油馏分的脱硫方法包括至少第一步骤A,用于使所述汽油馏分与酸容量大于4.7当量/ kg的酸性树脂接触 比表面积小于55m2 / g,第二步骤B从第一步骤中分离出混合物。

    Enhanced solvent deasphalting process for heavy hydrocarbon feedstocks utilizing solid adsorbent
    20.
    发明申请
    Enhanced solvent deasphalting process for heavy hydrocarbon feedstocks utilizing solid adsorbent 有权
    使用固体吸附剂的重质烃原料的增强溶剂脱沥青方法

    公开(公告)号:US20080093260A1

    公开(公告)日:2008-04-24

    申请号:US11584771

    申请日:2006-10-20

    CPC classification number: C10G21/003 C10G25/00 C10G25/003 C10G25/05

    Abstract: A solvent deasphalting of crude oil or petroleum heavy fractions and residues is carried out in the presence of a solid adsorbent, such as clay, silica, alumina and activated carbon, which adsorbs the contaminants and permits the solvent and oil fraction to be removed as a separate stream from which the solvent is recovered for recycling; the adsorbent with contaminants and the asphalt bottoms is mixed with aromatic and/or polar solvents to desorb the contaminants and washed as necessary, e.g., with benzene, toluene, xylenes and tetrahydrofuran, to clean adsorbant which is recovered and recycled; the solvent-asphalt mixture is sent to a fractionator for recovery and recycling of the aromatic or polar solvent. The bottoms from the fractionator include the concentrated PNA and contaminants and are further processes as appropriate.

    Abstract translation: 原油或石油重馏分和残余物的溶剂脱沥青在固体吸附剂如粘土,二氧化硅,氧化铝和活性炭的存在下进行,其吸附污染物并允许将溶剂和油馏分作为 回收溶剂的回收分离物流; 具有污染物的吸附剂和沥青底部物质与芳族和/或极性溶剂混合以解吸污染物并根据需要例如用苯,甲苯,二甲苯和四氢呋喃洗涤以清洁回收和再循环的吸附剂; 将溶剂 - 沥青混合物送至分馏器以回收和再循环芳族或极性溶剂。 来自分馏器的塔底物包括浓缩的PNA和污染物,并且是适当的进一步的方法。

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