PROCESS FOR TREATING A HEAVY HYDROCARBON FEEDSTOCK TO REDUCE ITS VISCOSITY
    2.
    发明申请
    PROCESS FOR TREATING A HEAVY HYDROCARBON FEEDSTOCK TO REDUCE ITS VISCOSITY 审中-公开
    处理重型油料进料以降低粘度的方法

    公开(公告)号:WO2010069907A1

    公开(公告)日:2010-06-24

    申请号:PCT/EP2009/067046

    申请日:2009-12-14

    CPC classification number: E21B43/16 C10G29/02

    Abstract: A process for reducing the viscosity a heavy hydrocarbon feedstock, comprising: supplying the heavy hydrocarbon feedstock and elemental sulphur to a reaction zone and reacting, in the liquid phase, at a temperature in the range of from 300 to 750°C, a part of the heavy hydrocarbon feedstock with the elemental sulphur to form a reaction mixture comprising heavy hydrocarbon stream, carbon disulphide and hydrogen sulphide, followed by cooling the reaction mixture to provide treated heavy hydrocarbon stream comprising carbon disulphide. The invention also concerns products obtainable by the above process, as well as its use in pipeline transportation.

    Abstract translation: 一种用于降低重烃原料的粘度的方法,包括:将重质烃原料和元素硫供应到反应区,并在液相中在300-750℃的温度范围内反应, 重质烃原料与元素硫形成包含重烃流,二硫化碳和硫化氢的反应混合物,然后冷却反应混合物以提供包含二硫化碳的经处理的重质烃流。 本发明还涉及通过上述方法可获得的产品,以及其在管道输送中的应用。

    SHAPED CATALYST PARTICLES FOR HYDROCARBON SYNTHESIS
    4.
    发明申请
    SHAPED CATALYST PARTICLES FOR HYDROCARBON SYNTHESIS 审中-公开
    用于烃合成的形状催化剂颗粒

    公开(公告)号:WO2003103833A1

    公开(公告)日:2003-12-18

    申请号:PCT/EP2003/006114

    申请日:2003-06-06

    Abstract: Shaped catalyst or catalyst precursor containing a catalytically active component or a precursor therefor, the component selected from elements of Group VIII of the Periodic Table of the Elements, supported on a carrier, which catalyst or catalyst precursor is an elongated shaped particle comprising three protrusions each extending from and attached to a central position, wherein the central position is aligned along the longitudinal axis of the particle, the cross-section of the particle occupying the space encompassed by the outer edges of six circles around a central circle, each of the six circles touching two neighbouring circles whilst three alternating circles are equidistant to the central circle and may be attached to the central circle, minus the space occupied by the three remaining outer circles and including the six interstitial regions. The invention further relates to a process to prepare the catalyst or catalyst precursor from a shapeable dough, to the die-plate used for the preparation of an extruded catalyst or catalyst precursor, to the use of the catalysts, as well as to hydrocarbons prepared by using the catalyst. The invention further relates to a process to obtain fuels and optionally base oils, by hydrogenation, hydroisomerisation and/or hydrocracking of the hydrocarbons prepared by using the catalyst.

    Abstract translation: 含有催化活性组分或其前体的成形催化剂或催化剂前体,选自负载在载体上的元素周期表第Ⅷ族的元素,该催化剂或催化剂前体是细长形状的颗粒,每个颗粒包含三个突起 从中心位置延伸并附接到中心位置,其中中心位置沿着颗粒的纵向轴线对齐,颗粒的横截面占据由围绕中心圆的六个圆的外边缘包围的空间,六个 接触两个相邻圆的圆,而三个交替的圆与中心圆等距,并且可以附接到中心圆,减去三个剩余的外圆占据的空间,并包括六个间隙区。 本发明还涉及一种从可成型面团制备催化剂或催化剂前体的方法,用于制备挤出的催化剂或催化剂前体的模板,使用催化剂以及由 使用催化剂。 本发明还涉及通过使用催化剂制备的烃的氢化,加氢异构化和/或加氢裂解来获得燃料和任选的基础油的方法。

    A PROCESS FOR THE MANUFACTURE OF CARBON DISULPHIDE
    9.
    发明申请
    A PROCESS FOR THE MANUFACTURE OF CARBON DISULPHIDE 审中-公开
    碳化硼制造工艺

    公开(公告)号:WO2007131977A1

    公开(公告)日:2007-11-22

    申请号:PCT/EP2007/054613

    申请日:2007-05-14

    CPC classification number: E21B43/16 C01B32/70 C09K8/58

    Abstract: The invention provides a process for the manufacture of carbon disulphide comprising supplying a molecular oxygen-containing gas and a feedstock comprising a hydrocarbonaceous compound to a reaction zone containing a liquid elemental sulphur phase and reacting, in the liquid sulphur phase, at a temperature in the range of from 300 to 750 °C, the hydrocarbonaceous compound with elemental sulphur to form carbon disulphide and hydrogen sulphide and oxidising at least part of the hydrogen sulphide formed to elemental sulphur and water. The invention further provides the use of a liquid stream comprising carbon disulphide, hydrogen sulphide and carbonyl sulphide obtainable such process for enhanced oil recovery.

    Abstract translation: 本发明提供了一种制造二硫化碳的方法,包括将含分子氧的气体和包含烃类化合物的原料供给到含有液体元素硫相的反应区中,并在液相硫相中在 范围为300至750℃,含烃化合物与元素硫形成二硫化碳和硫化氢,并将至少部分硫化氢氧化成元素硫和水。 本发明进一步提供了包含二硫化碳,硫化氢和羰基硫化物的液体流的用途,这种方法可用于提高采油率。

    PROCESS FOR PRODUCING A GAS STREAM DEPLETED OF HYDROGEN SULPHIDE
    10.
    发明申请
    PROCESS FOR PRODUCING A GAS STREAM DEPLETED OF HYDROGEN SULPHIDE 审中-公开
    用于生产排出硫化氢的气流的方法

    公开(公告)号:WO2006103217A1

    公开(公告)日:2006-10-05

    申请号:PCT/EP2006/061073

    申请日:2006-03-28

    CPC classification number: C01B17/54 B01D53/8612 C01B17/0469 C01B17/05

    Abstract: The invention provides a process for producing a gas stream depleted of H 2 S from a feed gas stream comprising H 2 S, the process comprising the steps of: (a) selectively oxidizing H 2 S by supplying the feed gas stream comprising H 2 S, an inert liquid medium and a molecular-oxygen comprising gas stream to a reaction zone comprising at least one catalytic zone comprising an oxidation catalyst and contacting the oxidation catalyst of each catalytic zone with the feed gas stream and/or the molecular-oxygen comprising gas stream in the presence of inert liquid medium at a temperature in the range of from 120 to 160 °C to form elemental sulphur and the gas stream depleted of H 2 S, under such conditions that the elemental sulphur formed is essentially in liquid form and is removed from the reaction zone with inert liquid medium to obtain a liquid stream comprising inert liquid medium and essentially liquid elemental sulphur; (b) optionally separating the liquid stream obtained in step (a) into a first liquid phase enriched in inert liquid medium and a second liquid phase enriched in liquid elemental sulphur; (c) combusting at least part of the liquid stream obtained in step (a) or at least part of the second liquid phase obtained in step (b) to form a fluid stream comprising sulphur dioxide.

    Abstract translation: 本发明提供了一种从包含H 2 S的进料气流产生缺乏H 2 S的气流的方法,该方法包括以下步骤:(a)选择性地 通过将包含H 2 S的惰性液体介质和包含分子氧的气流供应到包含至少一种催化剂的反应区域来氧化H 2 S 区,其包含氧化催化剂,并且在惰性液体介质存在下,在120至160℃的温度范围内将每个催化区的氧化催化剂与进料气流和/或含分子氧的气流接触,温度范围为120至160℃至 在形成的元素硫基本上是液体形式并且用惰性液体介质从反应区中除去以获得液体流的条件下,形成元素硫和不饱和H 2 S的气流,以获得包含 惰性液体介质和基本上液体的元素硫; (b)任选地将步骤(a)中获得的液体流分离成富含惰性液体介质的第一液相和富含液体元素硫的第二液相; (c)将步骤(a)中获得的至少部分液体物流或步骤(b)中获得的至少部分第二液相燃烧以形成包含二氧化硫的流体物流。

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