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    SYSTEM FOR BLENDING SYNTHETIC AND NATURAL CRUDE OILS DERIVED FROM OFFSHORE PRODUCED FLUIDS
    2.
    发明申请
    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系统

    公开(公告)号：US20140241952A1

    公开(公告)日：2014-08-28

    申请号：US14267211

    申请日：2014-05-01

    申请人： Charles Leonard Kibby ,  Dennis John O'Rear ,  Robert James Saxton ,  Tapan Kumar Das ,  Kandaswany Jothimurugesan

    发明人： Charles Leonard Kibby ,  Dennis John O'Rear ,  Robert James Saxton ,  Tapan Kumar Das ,  Kandaswany Jothimurugesan

    IPC分类号： C10G2/00

    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 and system for blending synthetic and natural crude oils derived from offshore produced fluids
    6.
    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
    7.
    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。

    PROCESSES AND SYSTEMS FOR SYNTHESIS GAS CONVERSION USING A HYBRID FISCHER-TROPSCH CATALYST IN A COMPACT HEAT EXCHANGE REACTOR
    9.
    发明申请
    PROCESSES AND SYSTEMS FOR SYNTHESIS GAS CONVERSION USING A HYBRID FISCHER-TROPSCH CATALYST IN A COMPACT HEAT EXCHANGE REACTOR 有权
    使用混合热交换催化剂在合成热交换反应器中合成气体转化的方法和系统

    公开(公告)号：US20140343175A1

    公开(公告)日：2014-11-20

    申请号：US14219774

    申请日：2014-03-19

    申请人： Robert James Saxton, JR. ,  Kandaswamy Jothimurugesan ,  Charles Leonard Kibby

    发明人： Robert James Saxton, JR. ,  Kandaswamy Jothimurugesan ,  Charles Leonard Kibby

    IPC分类号： C07C1/04

    CPC分类号： C07C1/0435 ,  B01J8/008 ,  B01J19/00 ,  B01J19/0093 ,  B01J23/75 ,  B01J23/8913 ,  B01J29/00 ,  B01J29/7669 ,  B01J35/0006 ,  B01J35/023 ,  B01J35/1019 ,  B01J2208/00026 ,  B01J2219/00049 ,  B01J2219/00761 ,  B01J2219/00783 ,  B01J2219/00822 ,  B01J2219/00826 ,  B01J2219/00835 ,  B01J2219/00873 ,  B01J2229/186 ,  C07C1/042 ,  C10G2/334 ,  F28D9/00 ,  F28D9/0062 ,  F28F3/00 ,  F28F3/025

    摘要： Disclosed are a process and a system for synthesis gas conversion. The process includes contacting a synthesis gas feed of hydrogen and carbon monoxide having a H2/CO ratio from 0.5 to 3.0 with a hybrid catalyst of particles having a particle size from 50 to 500 μm and having at least one zeolite and a Fischer-Tropsch component wherein the ratio of zeolite to Fischer-Tropsch component is from 0.1:1 to 30:1 and the hybrid catalyst includes from 0.5 to 40 wt % Fischer-Tropsch component. The process is conducted in a compact heat exchange reactor having a set of reaction passages disposed between a synthesis gas feed header and a products header and a set of coolant passages disposed between a coolant inlet header and a coolant outlet header. The set of coolant passages conducts a coolant therethrough, and the set of reaction passages contains the hybrid catalyst therein and conducts synthesis gas and reaction products therethrough. The process is conducted at a temperature from 200 to 2800° C., a pressure from 5 to 40 atmospheres, a recycle ratio from 1 to 3, and a gaseous hourly space velocity less than 20,000 volumes of gas per volume of catalyst per hour. The effluent produced includes a hydrocarbon product containing at least 50 wt % C5+ hydrocarbons and less than 5 wt % C21+ hydrocarbons at a C5+ productivity from 0.05 to 2 gC5+/gcat/h.

    摘要翻译： 公开了合成气转化的方法和系统。 该方法包括将H 2 / CO比为0.5至3.0的氢气和一氧化碳的合成气进料与粒度为50-500μm的颗粒的混合催化剂接触并具有至少一种沸石和费 - 托组分 其中沸石与费 - 托组分的比例为0.1:1至30:1，并且所述混合催化剂包含0.5至40wt％的费 - 托组分。 该过程在紧凑的热交换反应器中进行，其具有设置在合成气进料集管和产品集管之间的一组反应通道和设置在冷却剂入口集管和冷却剂出口集管之间的一组冷却剂通道。 该组冷却剂通道使冷却剂通过其中，并且该组反应通道在其中包含混合催化剂，并通过其引导合成气和反应产物。 该方法在200至2800℃的温度，5至40个大气压的压力，1至3的循环比和每小时体积的催化剂小于20,000体积的气体的气时空速下进行。 产生的流出物包含含有至少50重量％的C 5+烃和少于5重量％的C 21+烃的烃产物，其C5 +生产率为0.05至2gC5 + / gcat / h。

    ACETYLENE ENHANCED CONVERSION OF SYNGAS TO FISCHER-TROPSCH HYDROCARBON PRODUCTS
    10.
    发明申请
    ACETYLENE ENHANCED CONVERSION OF SYNGAS TO FISCHER-TROPSCH HYDROCARBON PRODUCTS 失效
    乙烯增强转化为FISCHER-TROPSCH碳氢化合物产品

    公开(公告)号：US20090170965A1

    公开(公告)日：2009-07-02

    申请号：US12342978

    申请日：2008-12-23

    申请人： Charles Leonard Kibby ,  Minquan Cheng

    发明人： Charles Leonard Kibby ,  Minquan Cheng

    IPC分类号： C07C27/04

    CPC分类号： C10G2/32 ,  C10G2300/304

    摘要： A method is disclosed for converting syngas to Fischer-Tropsch (F-T) hydrocarbon products. A synthesis gas including carbon monoxide and hydrogen gas is provided to a F-T reactor. Also, acetylene is supplied to the F-T reactor. The ratio of the volume of acetylene to the volume of synthesis gas is at least 0.01. The synthesis gas and acetylene are reacted under suitable reaction conditions and in the presence of a catalyst to produce F-T hydrocarbon products. The F-T hydrocarbon products are then recovered from the reactor. The synthesis gas and acetylene may be provided in a combined feed stream or introduced separately into the reactor. The acetylene enhanced syngas conversion in a F-T reactor results in the synthesis of F-T products which have a tighter distribution of intermediate length carbon products than do F-T products synthesized according to conventional methods.

    摘要翻译： 公开了将合成气转化为费 - 托（F-T）烃产物的方法。 将包含一氧化碳和氢气的合成气体提供给F-T反应器。 此外，向F-T反应器供应乙炔。 乙炔体积与合成气体积之比至少为0.01。 合成气和乙炔在合适的反应条件下和催化剂存在下反应生成F-T烃产物。 然后从反应器中回收F-T烃产物。 合成气和乙炔可以以组合的进料流提供或分开引入反应器。 在F-T反应器中乙炔增强的合成气转化导致F-T产物的合成，其具有与根据常规方法合成的F-T产物相比中等长度碳产物分布更严格的F-T产物。