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公开(公告)号：US20140166281A1
公开(公告)日：2014-06-19
申请号：US14102767
申请日：2013-12-11
Applicant: CONOCOPHILLIPS COMPANY
Inventor： David W. LARKIN , Peter N. SLATER , Christopher R. COPELAND , Richard D. SADOK
IPC: E21B43/24
CPC classification number: E21B43/2406 , F22B1/167
Abstract: Systems and methods generate steam in hydrocarbon recovery operations and may further enable emulsion separation and product upgrading. The methods rely on indirect boiling of water by contact with a thermal transfer liquid heated to a temperature sufficient to vaporize the water. Examples of the liquid include oils, recovered hydrocarbons, liquid metals and brine. Heating of the liquid may utilize circulation of the liquid across or through a furnace, heat exchangers, or a gas-liquid contactor supplied with hot gas. Further, a solvent for bitumen introduced into the water may also vaporize upon contact with the thermal transfer liquid.
Abstract translation: 系统和方法在烃回收操作中产生蒸汽，并且可以进一步实现乳液分离和产物升级。 该方法依赖于通过与加热到足以蒸发水的温度的热转印液接触来间接沸腾水。 液体的实例包括油，回收的烃，液态金属和盐水。 液体的加热可利用液体在炉子，热交换器或供应有热气体的气液接触器之间或之间的循环。 此外，引入水中的沥青的溶剂也可以在与热转印液体接触时蒸发。
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公开(公告)号：US20230084729A1
公开(公告)日：2023-03-16
申请号：US17879014
申请日：2022-08-02
Applicant: CONOCOPHILLIPS COMPANY
Inventor： Peter N. SLATER
Abstract: Methods for reducing or reusing emissions and waste from oil and gas processing facilities are described. Specifically, emission and waste streams can be partially oxidized before being treated in a modified syngas fermentation process with parallel bioreactors to produce commodity chemicals of commercial importance while lowering greenhouse gas emissions. At least one bioreactor is online at all times, offline reactors being emptied to collect product and recharged for use.
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公开(公告)号：US20140165928A1
公开(公告)日：2014-06-19
申请号：US14095705
申请日：2013-12-03
Applicant: CONOCOPHILLIPS COMPANY
Inventor： David W. LARKIN , Scott D. LOVE , Scott MACADAM , Peter N. SLATER , Edward G. LATIMER , Richard B. MILLER
IPC: F22B1/02
Abstract: Systems and methods relate to vaporizing water into steam, which may be utilized in applications such as bitumen production. The methods rely on indirect boiling of the water by contact with a substance such as solid particulate heated to a temperature sufficient to vaporize the water. Heating of the solid particulate may utilize pressure isolated heat exchanger units or a hot gas recirculation circuit at a pressure corresponding to that desired for the steam. Further, the water may form part of a mixture that contacts the solid particulate and includes a solvent for the bitumen in order to limit vaporization energy requirements and facilitate the production.
Abstract translation: 系统和方法涉及将水蒸发成蒸汽，其可用于诸如沥青生产的应用中。 这些方法依赖于通过与加热到足以蒸发水的温度的物质如固体颗粒接触来间接沸腾水。 固体颗粒的加热可以在与蒸汽所需的压力相对应的压力下使用压力分离的热交换器单元或热气体再循环回路。 此外，水可以形成与固体颗粒接触的混合物的一部分，并且包括用于沥青的溶剂，以限制蒸发能量需求并促进生产。
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Patent Agency Ranking
公开(公告)号：US20180328156A1
公开(公告)日：2018-11-15
申请号：US15978925
申请日：2018-05-14
Applicant: CONOCOPHILLIPS COMPANY
Inventor： Peter N. SLATER
CPC classification number: E21B43/2408 , E21B37/06 , E21B43/34
Abstract: SAGD equipment including steam generating equipment may be cleaned using supercritical carbon dioxide. Supercritical carbon dioxide is a fluid state of carbon dioxide where it is held at or above its critical temperature and critical pressure. Supercritical carbon dioxide has exceptional solvent qualities that can dissolve, soften, or dislodge the refractory fouling deposits in the SAGD equipment.
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公开(公告)号：US20140165930A1
公开(公告)日：2014-06-19
申请号：US14097496
申请日：2013-12-05
Applicant: CONOCOPHILLIPS COMPANY
Inventor： David W. LARKIN , Scott D. LOVE , Scott MACADAM , Peter N. SLATER
IPC: F22B1/02
CPC classification number: F22B1/028
Abstract: Systems and methods relate to vaporizing water into steam, which may be utilized in applications such as bitumen production. The methods rely on indirect boiling of the water by contact with a substance such as solid particulate heated to a temperature sufficient to vaporize the water. Heating of the solid particulate may utilize pressure isolated heat exchanger units or a hot gas recirculation circuit at a pressure corresponding to that desired for the steam. Further, the water may form part of a mixture that contacts the solid particulate and includes a solvent for the bitumen in order to limit vaporization energy requirements and facilitate the production.
Abstract translation: 系统和方法涉及将水蒸发成蒸汽，其可用于诸如沥青生产的应用中。 这些方法依赖于通过与加热到足以蒸发水的温度的物质如固体颗粒接触来间接沸腾水。 固体颗粒的加热可以在与蒸汽所需的压力相对应的压力下使用压力分离的热交换器单元或热气体再循环回路。 此外，水可以形成与固体颗粒接触的混合物的一部分，并且包括用于沥青的溶剂，以限制蒸发能量需求并促进生产。
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公开(公告)号：US20150096754A1
公开(公告)日：2015-04-09
申请号：US14510548
申请日：2014-10-09
Applicant: CONOCOPHILLIPS COMPANY
Inventor： David W. LARKIN , Peter N. SLATER , Kening GONG
CPC classification number: E21B43/24 , E21B43/2406 , F22B33/14 , F22D11/006
Abstract: Systems and methods relate to vaporizing water into steam, which may be utilized in applications such as bitumen production. Initial indirect vaporization of the water at a first pressure for treatment precedes a steam generator boiling the water at a second pressure higher than the first pressure. The indirect vaporization of the water occurs in a vessel upon contact of the water with a substance such as solid particulate heated to a temperature sufficient to vaporize the water. Impurities in the water deposit on the solid particulate and/or combust limiting pass through of the impurities to the steam generator given that a vapor output of the vessel from the initial indirect vaporization condenses and is pressurized before being supplied to the steam generator.
Abstract translation: 系统和方法涉及将水蒸发成蒸汽，其可用于诸如沥青生产的应用中。 在处理第一压力下的水的初始间接蒸发先于蒸汽发生器在高于第一压力的第二压力下沸腾水。 当水与物质如固体颗粒接触时，水的间接蒸发发生在容器中，该物质被加热至足以蒸发水的温度。 考虑到容器从初始间接蒸发的蒸汽输出在供给到蒸汽发生器之前会被冷凝并被加压，固体颗粒中的水沉积物中的杂质和/或燃烧限制通过杂质到蒸汽发生器。
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公开(公告)号：US20140166538A1
公开(公告)日：2014-06-19
申请号：US14095444
申请日：2013-12-03
Applicant: CONOCOPHILLIPS COMPANY
Inventor： David W. LARKIN , Peter N. SLATER , Richard D. SADOK
IPC: C10G33/00
Abstract: Systems and methods generate steam in hydrocarbon recovery operations and may further enable emulsion separation and product upgrading. The methods rely on indirect boiling of water by contact with a thermal transfer liquid heated to a temperature sufficient to vaporize the water. Examples of the liquid include oils, recovered hydrocarbons, liquid metals and brine. Heating of the liquid may utilize circulation of the liquid across or through a furnace, heat exchangers, or a gas-liquid contactor supplied with hot gas. Further, a solvent for bitumen introduced into the water may also vaporize upon contact with the thermal transfer liquid.
Abstract translation: 系统和方法在烃回收操作中产生蒸汽，并可进一步实现乳液分离和产品升级。 该方法依赖于通过与加热到足以蒸发水的温度的热转印液接触来间接沸腾水。 液体的实例包括油，回收的烃，液态金属和盐水。 液体的加热可利用液体在炉子，热交换器或供应有热气体的气液接触器之间或之间的循环。 此外，引入水中的沥青的溶剂也可以在与热转印液体接触时蒸发。
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公开(公告)号：US20140166263A1
公开(公告)日：2014-06-19
申请号：US14097695
申请日：2013-12-05
Applicant: CONOCOPHILLIPS COMPANY
Inventor： Peter N. SLATER , Christopher R. COPELAND
IPC: E21B43/24
CPC classification number: E21B43/2406 , E21B43/34 , F22B3/04 , F22B33/18 , F22B37/486
Abstract: Systems and methods generate steam in hydrocarbon recovery operations and may further enable emulsion separation and product upgrading. The methods rely on indirect boiling of water by contact with a thermal transfer liquid heated to a temperature sufficient to vaporize the water. Examples of the liquid include oils, recovered hydrocarbons, liquid metals and brine. Heating of the liquid may utilize circulation of the liquid across or through a furnace, heat exchangers, or a gas-liquid contactor supplied with hot gas. Further, a solvent for bitumen introduced into the water may also vaporize upon contact with the thermal transfer liquid.
Abstract translation: 系统和方法在烃回收操作中产生蒸汽，并可进一步实现乳液分离和产品升级。 该方法依赖于通过与加热到足以蒸发水的温度的热转印液接触来间接沸腾水。 液体的实例包括油，回收的烃，液态金属和盐水。 液体的加热可利用液体在炉子，热交换器或供应有热气体的气液接触器之间或之间的循环。 此外，引入水中的沥青的溶剂也可以在与热转印液体接触时蒸发。
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