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    Process and system for blending synthetic and natural crude oils derived from offshore produced fluids
    3.
    发明授权
    Process and system for blending synthetic and natural crude oils derived from offshore produced fluids 有权
    用于混合源自海上生产流体的合成和天然原油的方法和系统

    公开(公告)号：US08753500B2

    公开(公告)日：2014-06-17

    申请号：US12974337

    申请日：2010-12-21

    申请人： Charles Leonard Kibby ,  Dennis J. O'Rear ,  Robert James Saxton ,  Tapan K. Das ,  Kandaswamy Jothimurugesan

    发明人： Charles Leonard Kibby ,  Dennis J. O'Rear ,  Robert James Saxton ,  Tapan K. Das ,  Kandaswamy Jothimurugesan

    IPC分类号： C10B57/02

    CPC分类号： C10G2/34 ,  C10G2/32 ,  C10G2/332 ,  C10G2/333 ,  C10G2/341 ,  C10G2/344 ,  C10G5/06 ,  C10G45/02 ,  C10G45/58 ,  C10G47/00 ,  C10G49/00 ,  C10G2300/1022 ,  C10G2300/1033 ,  C10G2300/302 ,  C10G2300/4062

    摘要： A process and system are described for the processing of gas associated with crude oil production, i.e. associated gas. A separation complex is used to separate produced fluids produced from a hydrocarbon reservoir into crude oil, liquefied petroleum gas, water, and natural gas. At least a portion of the natural gas is converted into synthesis gas in a synthesis gas generator. A combination of a synthesis gas conversion catalysts and hydroconversion catalysts are used in a synthesis gas reactor to convert the synthesis gas into a liquid effluent stream containing liquefied petroleum gas and a synthetic crude oil. The liquefied petroleum gas and synthetic crude oil from the synthesis gas reactor is sent to the separation complex. Liquefied petroleum gas is separated both from the synthetic crude oil and a natural crude oil obtained from the produced fluids. The system and process permits synthetic crude oil to be blended with the natural crude oil producing a blended stabilized crude oil having 2 wt % or more of the synthetic crude oil and with a pour point of 60° C. or less. Use of a common facility for separation operations on the natural crude oil and synthetic crude oil thus reduces capital costs and allows converted associated gases to be shipped with the natural crude oil on a conventional crude oil tanker.

    摘要翻译： 描述了用于处理与原油生产相关的气体，即相关气体的方法和系统。 分离复合物用于将由烃储层产生的产物分离成原油，液化石油气，水和天然气。 至少一部分天然气在合成气发生器中被转化为合成气。 在合成气反应器中使用合成气转化催化剂和加氢转化催化剂的组合，以将合成气转化为含有液化石油气和合成原油的液体流出物流。 将来自合成气反应器的液化石油气和合成原油送至分离复合物。 液化石油气与合成原油和从生产的流体获得的天然原油分离。 该系统和方法允许合成原油与天然原油混合，产生具有2重量％或更多的合成原油并且倾点为60℃或更低的混合稳定的原油。 在天然原油和合成原油上使用通用设施进行分离操作，从而降低资本成本，并允许转换的相关气体与常规原油油轮上的天然原油一起运输。

    PROCESS AND SYSTEM FOR BLENDING SYNTHETIC AND NATURAL CRUDE OILS DERIVED FROM OFFSHORE PRODUCED FLUIDS
    6.
    发明申请
    PROCESS AND SYSTEM FOR BLENDING SYNTHETIC AND NATURAL CRUDE OILS DERIVED FROM OFFSHORE PRODUCED FLUIDS 有权
    从海洋生产的流体中混合合成和自然原油的方法和系统

    公开(公告)号：US20110240288A1

    公开(公告)日：2011-10-06

    申请号：US12974337

    申请日：2010-12-21

    申请人： Charles Leonard Kibby ,  Dennis J. O'Rear ,  Robert James Saxton ,  Tapan K. Das ,  Kandaswamy Jothimurugesan

    发明人： Charles Leonard Kibby ,  Dennis J. O'Rear ,  Robert James Saxton ,  Tapan K. Das ,  Kandaswamy Jothimurugesan

    IPC分类号： E21B43/00

    CPC分类号： C10G2/34 ,  C10G2/32 ,  C10G2/332 ,  C10G2/333 ,  C10G2/341 ,  C10G2/344 ,  C10G5/06 ,  C10G45/02 ,  C10G45/58 ,  C10G47/00 ,  C10G49/00 ,  C10G2300/1022 ,  C10G2300/1033 ,  C10G2300/302 ,  C10G2300/4062

    摘要： A process and system are described for the processing of gas associated with crude oil production, i.e. associated gas. A separation complex is used to separate produced fluids produced from a hydrocarbon reservoir into crude oil, liquefied petroleum gas, water, and natural gas. At least a portion of the natural gas is converted into synthesis gas in a synthesis gas generator. A combination of a synthesis gas conversion catalysts and hydroconversion catalysts are used in a synthesis gas reactor to convert the synthesis gas into a liquid effluent stream containing liquefied petroleum gas and a synthetic crude oil. The liquefied petroleum gas and synthetic crude oil from the synthesis gas reactor is sent to the separation complex. Liquefied petroleum gas is separated both from the synthetic crude oil and a natural crude oil obtained from the produced fluids. The system and process permits synthetic crude oil to be blended with the natural crude oil producing a blended stabilized crude oil having 2 wt % or more of the synthetic crude oil and with a pour point of 60° C. or less. Use of a common facility for separation operations on the natural crude oil and synthetic crude oil thus reduces capital costs and allows converted associated gases to be shipped with the natural crude oil on a conventional crude oil tanker.

    摘要翻译： 描述了用于处理与原油生产相关的气体，即相关气体的方法和系统。 分离复合物用于将由烃储层产生的产物分离成原油，液化石油气，水和天然气。 至少一部分天然气在合成气发生器中被转化为合成气。 在合成气反应器中使用合成气转化催化剂和加氢转化催化剂的组合，以将合成气转化为含有液化石油气和合成原油的液体流出物流。 将来自合成气反应器的液化石油气和合成原油送至分离复合物。 液化石油气与合成原油和从生产的流体获得的天然原油分离。 该系统和方法允许合成原油与天然原油混合，产生具有2重量％或更多的合成原油并且倾点为60℃或更低的混合稳定的原油。 在天然原油和合成原油上使用通用设施进行分离操作，从而降低资本成本，并允许转换的相关气体与常规原油油轮上的天然原油一起运输。

    Process for extracting bitumen using light oil
    8.
    发明授权
    Process for extracting bitumen using light oil 有权
    使用轻油提取沥青的方法

    公开(公告)号：US07837864B2

    公开(公告)日：2010-11-23

    申请号：US12004052

    申请日：2007-12-20

    申请人： Bruce E. Reynolds

    发明人： Bruce E. Reynolds

    IPC分类号： C10G1/04

    CPC分类号： C10G1/047 ,  C10G45/02 ,  C10G47/00 ,  C10G65/12 ,  C10G2300/4062

    摘要： An integrated process for extracting and refining bitumen comprises hydroconverting bitumen in a reactor to provide valuable products and light oil by-product; separating the light oil by-product from the valuable products; transporting the light oil to oil sands reserves; producing steam in steam generators at the oil sands reserves using a portion of the light oil transported to the oil sands reserves; extracting bitumen from the oil sands reserves using steam produced in the steam generators; blending bitumen extracted from the oil sands reserves and a portion of the light oil transported to the oil sands reserves to form a transport blend; and transporting the transport blend to the reactor.

    摘要翻译： 用于提炼和精制沥青的综合方法包括在反应器中加氢转化沥青以提供有价值的产物和轻质油副产物; 将轻油副产品与有价值产品分离; 运输轻油到油砂储备; 在油砂储备的蒸汽发生器中生产蒸汽，运送一部分运往油砂储量的轻油; 使用蒸汽发生器中产生的蒸汽从油砂储备中提取沥青; 将从油砂储备中提取的沥青和部分轻油输送到油砂储备中形成运输混合物; 并将运输混合物运输到反应器。

    Petroleum products from oil shale
    10.
    发明申请
    Petroleum products from oil shale 失效
    石油产品来自油页岩

    公开(公告)号：US20090095659A1

    公开(公告)日：2009-04-16

    申请号：US11974492

    申请日：2007-10-12

    申请人： Robert D. Morris, JR. ,  Robert D. Morris, III

    发明人： Robert D. Morris, JR. ,  Robert D. Morris, III

    IPC分类号： C10G1/04

    CPC分类号： C10G1/02 ,  C01B3/50 ,  C01B2203/04 ,  C01B2203/047 ,  C10B47/30 ,  C10B53/06 ,  C10B57/02 ,  C10G1/002 ,  C10G1/06 ,  C10G2300/4062 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/16 ,  C10J2300/1634

    摘要： A system for producing petroleum products from oil shale includes one or plural kiln lines made up of plural series-connected, indirect-fired, inclined rotary kilns. Plural kiln lines are operated for parallel processing. Oil shale is advanced through kilns in succession and exhausted from each kiln line substantially free of hydrocarbons. Successive kilns along the advancement of oil shale are maintained at successively higher temperatures. A fuel distinct from hydrocarbons in oil shale, such as syngas from a gasifier or hydrogen gas from a separator, drives pyrolysis to extract hydrocarbons. A refining unit located proximate to the kiln lines upgrades extracted hydrocarbons into petroleum products and separates the petroleum products by criteria. A heat extraction unit recovers heat from exhausted oil shale for reuse in kilns. A method involves drying oil shale followed by heating dry oil shale in successively hotter pyrolysis environments.

    摘要翻译： 用于从油页岩生产石油产品的系统包括由多个串联，间接燃烧的倾斜回转窑组成的一个或多个窑炉线。 多台窑线经过并行处理。 油页岩连续前进通过窑炉，并从基本上不含碳氢化合物的每个窑线排出。 沿着油页岩进展的连续窑炉依然保持较高的温度。 与油页岩中的碳氢化合物不同的燃料，例如来自气化器的合成气或来自分离器的氢气驱动热解提取烃。 位于窑道附近的精炼单元将提取的碳氢化合物升级成石油产品，并通过标准分离石油产品。 一个取热单元从排出的油页岩中回收热量，以便在窑炉中重新使用。 一种方法包括干燥油页岩，然后在相继较热的热解环境中加热干油页岩。