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公开(公告)号:US20130133337A1
公开(公告)日:2013-05-30
申请号:US13307646
申请日:2011-11-30
Applicant: Ahmed Mostafa ELKady , Uyigue Omoma Idahosa
Inventor: Ahmed Mostafa ELKady , Uyigue Omoma Idahosa
CPC classification number: F23L7/007 , F23C9/00 , F23J15/06 , F23L2900/07001 , F23L2900/07002 , F23L2900/07005 , F25J3/04533 , F25J3/04569 , F25J2260/80 , Y02E20/322 , Y02E20/344
Abstract: System and methods for hydrogen assisted oxy-fuel combustion are provided. The system includes a combustor, an air separation unit, a fuel stream source, and a condenser. The combustor includes an oxygen input port, a fuel stream input port, a carbon dioxide input port, and an exhaust output port. The air separation unit is in fluid communication with the combustor via the oxygen input port of the combustor. The fuel stream source is in fluid communication with the combustor via the fuel stream input port and includes a fuel source and a hydrogen source. The condenser is disposed to receive an exhaust from the combustor via the exhaust output port and to return an output stream to the combustor via the carbon dioxide input port. The method includes combusting a fuel stream in a combustor in the presence of an oxidizer to generate an exhaust gas.
Abstract translation: 提供了氢辅助氧燃料燃烧的系统和方法。 该系统包括燃烧器,空气分离单元,燃料流源和冷凝器。 燃烧器包括氧气输入端口,燃料流输入端口,二氧化碳输入端口和排气输出端口。 空气分离单元经由燃烧器的氧气输入端口与燃烧器流体连通。 燃料流源通过燃料流输入端口与燃烧器流体连通,并且包括燃料源和氢源。 冷凝器设置成经由排气输出端口接收来自燃烧器的排气并且经由二氧化碳输入端口将输出流返回到燃烧器。 该方法包括在氧化剂存在下在燃烧器中燃烧燃料流以产生废气。
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公开(公告)号:US20120023956A1
公开(公告)日:2012-02-02
申请号:US13217601
申请日:2011-08-25
Applicant: Predrag Popovic
Inventor: Predrag Popovic
CPC classification number: F02C3/34 , F01K23/10 , F05D2260/61 , F25J3/04018 , F25J3/04127 , F25J3/04533 , F25J3/04569 , F25J3/046 , F25J2260/80
Abstract: A power plant and method of operation is provided. The power plant comprises at least one main air compressor, an oxidizer unit configured to deliver a compressed oxygen-rich gas flow to at least one gas turbine assembly. Each assembly comprises a turbine combustor for mixing the compressed oxygen-rich gas flow with a recirculated gas flow and a fuel stream to burn a combustible mixture and form the recirculated gas flow. The assembly also comprises a recirculation loop for recirculating the recirculated gas flow from a turbine to a turbine compressor. The assembly further comprises a recirculated gas flow extraction path for extracting a portion of the recirculated gas flow from the assembly and delivering this to a gas separation system. The gas separation system separates the portion of the recirculated gas flow into a nitrogen portion and a carbon dioxide portion.
Abstract translation: 提供电厂和操作方法。 发电厂包括至少一个主空气压缩机,氧化器单元,其被构造成将压缩的富氧气体流输送到至少一个燃气轮机组件。 每个组件包括涡轮机燃烧器,用于将经压缩的富氧气体流与再循环气体流和燃料流混合以燃烧可燃混合物并形成再循环气体流。 组件还包括用于将再循环的气体流从涡轮再循环到涡轮压缩机的再循环回路。 组件还包括再循环气流提取路径,用于从组件中提取一部分再循环气体流并将其输送到气体分离系统。 气体分离系统将再循环气体的一部分分离成氮气部分和二氧化碳部分。
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公开(公告)号:US20060272813A1
公开(公告)日:2006-12-07
申请号:US10538418
申请日:2003-12-12
Applicant: Ola Olsvik , Erling Rytter , Jostein Sogge , Jan Stensen
Inventor: Ola Olsvik , Erling Rytter , Jostein Sogge , Jan Stensen
CPC classification number: E21B43/168 , E21B43/40 , F25J3/04539 , F25J3/04569 , F25J3/04575 , F25J3/04593
Abstract: A method for increasing oil recovery from an oil reservoir by injection of gas into the reservoir, is described. The method comprises separation of air into an oxygen-rich fraction and a nitrogen-rich fraction, reformation of natural gas together with oxygen to produce a synthesis gas for production of methanol or other oxygenated hydrocarbons or higher hydrocarbons. The raw synthesis products and a waste gas from the synthesis are separated, and the nitrogen-rich fraction and at least a part of the waste gas are injected into the oil reservoir to increase the oil recovery from the reservoir. A plant for performing the method is also described.
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14.
公开(公告)号:US07100692B2
公开(公告)日:2006-09-05
申请号:US10486806
申请日:2002-08-06
Applicant: Alan John Parsley , Christiaan Stouthamer
Inventor: Alan John Parsley , Christiaan Stouthamer
CPC classification number: C01B13/0248 , C01B3/36 , C01B2203/0255 , C01B2203/062 , C01B2210/0046 , C01B2210/0051 , C01B2210/0062 , C10G2/30 , E21B43/006 , E21B43/168 , F17C1/007 , F17C3/005 , F25J3/04539 , F25J3/04569
Abstract: A process for the recovery of oil from a subsurface reservoir in combination with the production of liquid hydrocarbons from a hydrocarbonaceous stream involving: (i) separating an oxygen/nitrogen mixture into a stream enriched in oxygen and an oxygen depleted stream; (ii) partial oxidation of the hydrocarbonaceous feed at elevated temperature and pressure using enriched oxygen produced in step (i) to produce synthesis gas; (iii) converting synthesis gas obtained in step (ii) into liquid hydrocarbons; and (iv) recovering oil from a subsurface reservoir using at least part of the oxygen depleted gas stream produced in step (i).
Abstract translation: 一种从地下储存器回收油的方法,其结合从烃流产生液态烃,其包括:(i)将氧/氮混合物分离成富含氧气和贫氧流的物流; (ii)在升高的温度和压力下使用在步骤(i)中产生的富氧氧气对含烃原料进行部分氧化以产生合成气; (iii)将步骤(ii)中获得的合成气转化成液体烃; 和(iv)使用步骤(i)中产生的至少部分氧耗尽的气流从地下贮存器回收油。
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公开(公告)号:US20050211440A1
公开(公告)日:2005-09-29
申请号:US11068437
申请日:2005-02-28
Applicant: Johannes Lanfermeijer , Herman Dijk
Inventor: Johannes Lanfermeijer , Herman Dijk
CPC classification number: F25J3/044 , F25J3/04018 , F25J3/0403 , F25J3/04133 , F25J3/04157 , F25J3/04296 , F25J3/04569 , F25J3/04987 , F25J2240/70 , F25J2240/82
Abstract: Nitrogen is produced above an offshore hydrocarbon reservoir (12) and injected into the reservoir, by a complex (40) mounted on a previously used vessel hull (16). The vessel weathervanes and the complex includes equipment that takes in ordinary air from a bow end (32) of the vessel, cools the air using sea water pumped into the equipment, and liquefies the oxygen component of air so pure nitrogen remains. The complex also includes injection equipment that heats and pressurizes the pure nitrogen to inject it into the reservoir. The complex is mounted above pipes (24) on the deck (22) of the vessel hull, on spacers (62) so mounting of equipment can be accomplished rapidly and without major alterations to the hull. A riser bundle (150) that extends from the hull to the sea floor, may include both a production riser (152) that carries crude hydrocarbons up to the vessel for storage in hull tanks (20), and an injection riser (160) that carries pressured nitrogen. The lower end of one of the risers is connected to a sea floor pipeline (162) that extends at least 100 meters away from the lower end of the other riser.
Abstract translation: 通过安装在先前使用的船体(16)上的复合物(40)将氮气在海上油气藏(12)上方产生并注入储层。 船舶风向标和复合体包括从容器的弓形端(32)吸收普通空气的设备,使用被泵送到设备中的海水冷却空气,并使空气的氧气成分液化,从而保持纯净的氮气。 该复合体还包括注射设备,其加热和加压纯氮以将其注入储存器。 复合体安装在容器船体的甲板(22)上的管道(24)上,在隔离件(62)上,因此可以快速实现设备的安装并且不会对船体造成重大变化。 从船体延伸到海底的提升管束(150)可以包括将粗烃运载到容器以存储在船体箱(20)内的生产提升管(152),以及注入提升管(160),其中 承受加压氮气。 提升管中的一个的下端连接到距离另一个提升管的下端至少100米延伸的海底管线(162)。
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16.
公开(公告)号:US20040244973A1
公开(公告)日:2004-12-09
申请号:US10486806
申请日:2004-07-09
Inventor: Alan John Parsley , Christiaan Stouthamer
IPC: E21B043/34
CPC classification number: C01B13/0248 , C01B3/36 , C01B2203/0255 , C01B2203/062 , C01B2210/0046 , C01B2210/0051 , C01B2210/0062 , C10G2/30 , E21B43/006 , E21B43/168 , F17C1/007 , F17C3/005 , F25J3/04539 , F25J3/04569
Abstract: A process for the recovery of oil from a subsurface reservoir in combination with the production of liquid hydrocarbons from a hydrocarbonaceous stream involving: (i) separating an oxygen/nitrogen mixture into a stream enriched in oxygen and an oxygen depleted stream; (ii) partial oxidation of the hydrocarbonaceous feed at elevated temperature and pressure using enriched oxygen produced in step (i) to produce synthesis gas; (iii) converting synthesis gas obtained in step (ii) into liquid hydrocarbons; and (iv) recovering oil from a subsurface reservoir using at least part of the oxygen depleted gas stream produced in step (i).
Abstract translation: 一种从地下储存器回收油的方法,其结合从烃流产生液态烃,其包括:(i)将氧/氮混合物分离成富含氧气和贫氧流的物流; (ii)在升高的温度和压力下使用在步骤(i)中产生的富氧氧气对含烃原料进行部分氧化以产生合成气; (iii)将步骤(ii)中获得的合成气转化成液体烃; 和(iv)使用步骤(i)中产生的至少部分氧耗尽的气流从地下贮存器回收油。
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17.
公开(公告)号:US6050105A
公开(公告)日:2000-04-18
申请号:US131979
申请日:1998-08-11
Applicant: Brian Anthony Keenan
Inventor: Brian Anthony Keenan
CPC classification number: F25J3/04018 , F25J3/0403 , F25J3/04121 , F25J3/04127 , F25J3/04139 , F25J3/04569 , F25J2240/82 , Y10S62/915
Abstract: An air separation plant includes a product nitrogen compressor, a gas turbine and a steam turbine. The gas turbine and the steam turbine are operatively associated with the product nitrogen compressor so as to be able to drive the product nitrogen compressor. The steam turbine has an inlet communicating with a steam generator adapted to recover heat from the gas turbine. The air separation plant also includes an air compressor which is typically similarly operatively associated with a gas turbine and a steam turbine. The steam turbine has an inlet communicating with a steam generator adapted to recover heat from the gas turbine.
Abstract translation: 空气分离设备包括氮气压缩机,燃气轮机和汽轮机。 燃气轮机和蒸汽轮机与产品氮压缩机可操作地相关联,以便能够驱动产品氮气压缩机。 蒸汽轮机具有与蒸汽发生器连通的入口,适于从燃气轮机回收热量。 空气分离设备还包括空气压缩机,其通常与燃气轮机和蒸汽涡轮机类似地操作地相关联。 蒸汽轮机具有与蒸汽发生器连通的入口,适于从燃气轮机回收热量。
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公开(公告)号:US08205455B2
公开(公告)日:2012-06-26
申请号:US13217601
申请日:2011-08-25
Applicant: Predrag Popovic
Inventor: Predrag Popovic
CPC classification number: F02C3/34 , F01K23/10 , F05D2260/61 , F25J3/04018 , F25J3/04127 , F25J3/04533 , F25J3/04569 , F25J3/046 , F25J2260/80
Abstract: A power plant and method of operation is provided. The power plant comprises at least one main air compressor, an oxidizer unit configured to deliver a compressed oxygen-rich gas flow to at least one gas turbine assembly. Each assembly comprises a turbine combustor for mixing the compressed oxygen-rich gas flow with a recirculated gas flow and a fuel stream to burn a combustible mixture and form the recirculated gas flow. The assembly also comprises a recirculation loop for recirculating the recirculated gas flow from a turbine to a turbine compressor. The assembly further comprises a recirculated gas flow extraction path for extracting a portion of the recirculated gas flow from the assembly and delivering this to a gas separation system. The gas separation system separates the portion of the recirculated gas flow into a nitrogen portion and a carbon dioxide portion.
Abstract translation: 提供电厂和操作方法。 发电厂包括至少一个主空气压缩机,氧化器单元,其被构造成将压缩的富氧气体流输送到至少一个燃气轮机组件。 每个组件包括涡轮机燃烧器,用于将经压缩的富氧气体流与再循环气体流和燃料流混合以燃烧可燃混合物并形成再循环气体流。 组件还包括用于将再循环的气体流从涡轮再循环到涡轮压缩机的再循环回路。 组件还包括再循环气流提取路径,用于从组件中提取一部分再循环气体流并将其输送到气体分离系统。 气体分离系统将再循环气体的一部分分离成氮气部分和二氧化碳部分。
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19.
公开(公告)号:US07168488B2
公开(公告)日:2007-01-30
申请号:US10487785
申请日:2002-08-30
Applicant: Ola Olsvik , Erling Rytter , Jostein Sogge , Rune Kvale , Sjur Haugen , Jan Grøntvedt
Inventor: Ola Olsvik , Erling Rytter , Jostein Sogge , Rune Kvale , Sjur Haugen , Jan Grøntvedt
CPC classification number: F25J3/04569 , C01B3/34 , C01B2203/0205 , C01B2203/0244 , C01B2203/0283 , C07C29/1518 , C10G2/30 , E21B43/168 , F25J3/04533 , F25J3/04539 , F25J3/04575 , F25J3/04593 , C07C31/04
Abstract: A method and a plant for simultaneous production of a gas for injection into an oil field and production of methanol, dimethyl ether and/or other oxygenated hydrocarbons or production of higher hydrocarbons from natural gas is disclosed. An air separation unit (ATR) for production of pure nitrogen for injection and pure oxygen for production of synthesis gas (“syngas”) by authermal reformation of a natural gas is an essential part of the method and plant.
Abstract translation: 公开了一种用于同时生产用于注入油田的气体并生产甲醇,二甲醚和/或其它含氧烃或从天然气生产高级烃的方法和设备。 用于生产注射纯氮的空气分离装置(ATR)和通过天然气的天然气改造生产合成气(“合成气”)的纯氧是该方法和装置的重要部分。
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公开(公告)号:US20060231455A1
公开(公告)日:2006-10-19
申请号:US10563991
申请日:2004-07-13
Applicant: Ola Olsvik , Kjell Moljord
Inventor: Ola Olsvik , Kjell Moljord
CPC classification number: F25J3/04569 , C01B3/382 , C01B3/386 , C01B3/52 , C01B32/50 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/0475 , C01B2203/065 , C01B2203/0844 , C01B2203/1241 , C01B2203/82 , C10G45/00 , C10G47/00 , C10G49/007 , E21B43/164 , E21B43/168 , E21B43/24 , E21B43/243 , F25J3/04018 , F25J3/04121 , F25J3/04539 , Y02C10/14 , Y02P20/125 , Y02P30/30 , Y02P90/70
Abstract: An integrated process for production and upgrading of heavy and extra-heavy crude oil, comprising (a) reforming of hydrocarbons such as natural gas to produce hydrogen, CO2 and steam (b) separating the produced hydrogen from the CO2, steam and any other gases to give a hydrogen rich fraction and a CO2 rich fraction and steam, (c) injecting the steam alone or in combination with the CO2 rich fraction into a reservoir containing heavy or extra heavy oil to increase the oil recovery, and (d) upgrading/refining of the heavy or extra heavy oil to finished products by extensive hydroprocessing, comprising several steps of hydrocracking and hydrotreating (sulfur, nitrogen and metals removal as well as hydrogenation of olefins and aromatics), using the hydrogen rich fraction.
Abstract translation: 包括(a)碳氢化合物如天然气的重整以产生氢气,二氧化碳和蒸汽(b)将所产生的氢气与二氧化碳,蒸气和任何其它气体分离出来的重和重质原油的生产和升级的综合方法 以提供富氢馏分和富CO2馏分和蒸汽,(c)将蒸汽单独或与富CO 2馏分组合注入含有重质或超重油的储层以增加油回收率,和(d)升级/ 通过广泛的加氢处理将重质或超重油精炼成成品,包括使用富氢馏分的几个步骤的加氢裂化和加氢处理(硫,氮和金属去除以及烯烃和芳族化合物的氢化)。
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