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公开(公告)号：US20160176793A1
公开(公告)日：2016-06-23
申请号：US14963344
申请日：2015-12-09
IPC分类号： C07C29/151 , C01B3/36 , C01B3/38
CPC分类号： C07C29/1518 , C01B3/36 , C01B3/382 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/061 , C01B2203/0872 , C01B2203/1258 , C01B2203/141 , C01B2203/142 , C01B2203/148 , C07C31/04
摘要： A method and system for producing methanol that employs steam methane reforming (SMR) and/or autothermal (ATR) synthesis gas production system, together with a partial oxidation system, is disclosed. The dual mode system and method for producing the synthesis gas in a methanol production process optimizes the efficiency and productivity of the methanol plant by using the partial oxidation based reforming system as an independent source of synthesis gas. The disclosed methods and systems are configurable either as a retrofit to existing methanol production facilities or as an integrated package into newly constructed methanol production facilities.
摘要翻译： 公开了一种使用蒸汽甲烷重整（SMR）和/或自热（ATR）合成气生产系统的甲醇生产方法和系统以及部分氧化系统。 在甲醇生产过程中用于生产合成气的双模系统和方法通过使用部分氧化基重整系统作为独立的合成气源来优化甲醇装置的效率和生产率。 公开的方法和系统可以作为对现有甲醇生产设施的改造或作为新建甲醇生产设备的综合包装进行配置。
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2.发明申请METHOD AND SYSTEM FOR PRODUCING A LIQUID HYDROCARBON PRODUCT FROM A FISCHER-TROPSCH PROCESS USING A SYNTHESIS GAS PRODUCED FROM AN OXYGEN TRANSPORT MEMBRANE BASED REFORMING REACTOR 有权使用由氧气输送膜生产的合成气基于改性反应器的FISCHER-TROPSCH工艺生产液体烃产品的方法和系统公开(公告)号：US20150251967A1
公开(公告)日：2015-09-10
申请号：US14638344
申请日：2015-03-04
CPC分类号： C07C1/04 , C01B3/382 , C01B3/384 , C01B13/0251 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0255 , C01B2203/062 , C01B2203/0811 , C01B2203/0838 , C01B2203/0844 , C01B2203/1241 , C01B2203/142
摘要： A system and method for producing a liquid hydrocarbon product from a Fischer-Tropsch process using a synthesis gas feed produced in an oxygen transport membrane based reforming reactor. The system and method involve reforming a mixed feed stream comprising natural gas, hydrogen and the Fischer-Tropsch tail gas, in a reforming reactor in the presence of steam, radiant heat from oxygen transport membrane elements and a reforming catalyst to produce a reformed synthesis gas stream comprising hydrogen, carbon monoxide, and unreformed hydrocarbon gas. The reformed synthesis gas stream is further reformed in an oxygen transport membrane based reforming reactor and conditioned to produce a synthesis gas product stream preferably having a H2/CO ratio of from about 1.7 to about 2.2. The synthesis gas product stream is then synthesized using a Fischer Tropsch process to produce the liquid hydrocarbon product and a Fischer-Tropsch tail gas.
摘要翻译： 一种使用在基于氧传输膜的重整反应器中生产的合成气进料从费 - 托方法生产液体烃产物的系统和方法。 该系统和方法包括在重整反应器中，在蒸汽存在的情况下重整包含天然气，氢气和费 - 托尾气的混合进料流，以及来自氧传输膜元件的辐射热和重整催化剂，以产生重整合成气 包含氢气，一氧化碳和未重整的烃气体。 将改性的合成气流在氧传输膜基重整反应器中进一步重整，并调节以产生优选具有约1.7至约2.2的H 2 / CO比的合成气产物流。 然后使用费托法合成合成气产物流，以产生液体烃产物和费 - 托尾气。
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3.发明申请公开(公告)号：US20120291351A1
公开(公告)日：2012-11-22
申请号：US13468189
申请日：2012-05-10
申请人： Lawrence Bool , Shrikar Chakravartt , Stefan E.F. Laux , Raymond F. Drnevich , Dante P. Bonaquist , David R. Thompson
发明人： Lawrence Bool , Shrikar Chakravartt , Stefan E.F. Laux , Raymond F. Drnevich , Dante P. Bonaquist , David R. Thompson
摘要： Oxygen is added to a raw syngas stream that contains hydrogen and CO, one or more light hydrocarbons, and that may also contain tars, produced by gasification of carbonaceous feed material, while imparting heat at a rate greater than 125 BTU per pound of oxygen added, to partially oxidize light hydrocarbons and convert tars if present to lower molecular weight products.
摘要翻译： 将氧气加入到含有氢气和CO，一种或多种轻质烃的原始合成气流中，并且还可以含有通过碳质进料的气化产生的焦油，同时以大于125BTU /磅的氧气加入热量 ，以部分氧化轻质烃并将焦油（如果存在）转化为较低分子量的产物。
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4.发明授权
公开(公告)号：US5557936A
公开(公告)日：1996-09-24
申请号：US508568
申请日：1995-07-27
申请人： Raymond F. Drnevich
发明人： Raymond F. Drnevich
CPC分类号： F01K25/065
摘要： A system for generating power as a result of an expansion of a pressurized working fluid through a turbine exhibits improved efficiency as the result of employing a tri-component working fluid that comprises water, ammonia and carbon dioxide. The pH of the working fluid is maintained within a range to prevent precipitation of carbon-bearing solids (preferably between 8.0 to 10.6). The working fluid enables an efficiency improvement in the Rankine cycle of up to 12 percent and an efficiency improvement in the Kalina cycle of approximately 5 percent.
摘要翻译： 由于使用包含水，氨和二氧化碳的三组分工作流体，由于加压工作流体通过涡轮膨胀而发电的系统表现出提高的效率。 工作流体的pH值保持在一定范围内，以防止含碳固体沉淀（优选在8.0至10.6之间）。 工作流体使兰金循环的效率提高达12％，卡利纳循环的效率提高约5％。
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公开(公告)号：US4834178A
公开(公告)日：1989-05-30
申请号：US205914
申请日：1988-06-13
IPC分类号： E21B43/16 , E21B43/243
CPC分类号： E21B43/162 , E21B43/243
摘要： A process and apparatus for fireflooding with liquid heat transfer media comprising injection of oxidant gas and liquid heat transfer media into a well through separate conduits, the liquid conduit downstream end submerged in a liquid volume, so as to form a seal and prevent oxidant gas migration into the liquid conduit.
摘要翻译： 一种用液体传热介质进行消火的方法和装置，包括将氧化剂气体和液体传热介质通过分开的导管注入井中，液体导管下游端浸没在液体体积中，以形成密封并防止氧化剂气体迁移 进入液体导管。
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6.发明授权Purge gas conditioning of high intensity ionization system for particle removal 失效用于除尘的高强度电离系统的吹扫气体调节
公开(公告)号：US4239505A
公开(公告)日：1980-12-16
申请号：US73297
申请日：1979-09-07
申请人： Raymond F. Drnevich
发明人： Raymond F. Drnevich
摘要： Back corona is controlled in high intensity ionization system for electrostatic charging of particles in gas stream by controlling purge gas flow and relative saturation content thereof.
摘要翻译： 背电晕在高强度电离系统中被控制，用于通过控制吹扫气体流量和相对饱和含量来对气流中的颗粒进行静电充电。
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公开(公告)号：US10787615B2
公开(公告)日：2020-09-29
申请号：US14166304
申请日：2014-01-28
摘要： The present invention relates to a method and system for treating a flow back fluid exiting a well site following stimulation of a subterranean formation. More specifically, the invention relates to processing the flow back fluid, and separating into a carbon dioxide rich stream and a carbon dioxide depleted stream, and continuing the separation until the carbon dioxide concentration in the flow back stream until the carbon dioxide concentration in the flow back gas diminishes to a point selected in a range of about 50-80 mol % in carbon dioxide concentration, after which the lower concentration carbon dioxide flow back stream continues to be separated into a carbon dioxide rich stream which is routed to waste or flare, and a hydrocarbon rich stream is formed.
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8.发明申请METHOD AND SYSTEM FOR PRODUCING A SYNTHESIS GAS USING AN OXYGEN TRANSPORT MEMBRANE BASED REFORMING SYSTEM WITH SECONDARY REFORMING AND AUXILIARY HEAT SOURCE 有权使用具有二次改造和辅助热源的基于氧气运输膜的改造系统生产合成气的方法和系统公开(公告)号：US20140323598A1
公开(公告)日：2014-10-30
申请号：US14261781
申请日：2014-04-25
IPC分类号： C07C29/151 , C07C29/152 , C01B3/02
CPC分类号： C01B3/384 , B01J19/245 , B01J19/2475 , B01J2219/00121 , B01J2219/00157 , B01J2219/24 , C01B3/02 , C01B3/382 , C01B3/386 , C01B13/0251 , C01B2203/0227 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/0822 , C01B2203/0827 , C01B2203/0838 , C01B2203/1235 , C01B2203/142 , C07C29/1518 , Y02P20/128 , C07C31/04
摘要： A method and system for producing a synthesis gas in an oxygen transport membrane based reforming system is disclosed that carries out a primary reforming process within a reforming reactor, and a secondary reforming process within an oxygen transport membrane reactor and in the presence of heat generated from a oxygen transport membrane reactor and an auxiliary source of heat. The auxiliary source of heat is disposed within the reactor housing proximate the reforming reactors and may include an auxiliary reactively driven oxygen transport membrane reactor or a ceramic burner.
摘要翻译： 公开了一种在基于氧传输膜的重整系统中生产合成气的方法和系统，其在重整反应器内进行初级重整过程，并在氧传输膜反应器内进行二次重整过程，并在存在由 氧传输膜反应器和辅助热源。 辅助热源在反应器壳体内靠近重整反应器设置，并且可以包括辅助的反应式驱动氧传输膜反应器或陶瓷燃烧器。
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公开(公告)号：US07985399B2
公开(公告)日：2011-07-26
申请号：US12056718
申请日：2008-03-27
IPC分类号： C01B3/26
CPC分类号： C01B3/12 , C01B3/384 , C01B3/48 , C01B3/52 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/0415 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/0811 , C01B2203/0822 , C01B2203/0894 , C01B2203/1258 , C01B2203/146 , C01B2203/148 , C10J3/00 , C10J3/466 , C10J3/82 , C10J2300/1621 , C10K1/004 , C10K1/005 , C10K3/04 , Y02P20/128
摘要： A hydrogen production method and facility in which a synthesis gas stream produced by the gasification of a carbonaceous substance is processed within a synthesis gas processing unit in which the carbon monoxide content is reacted with steam to produce additional hydrogen that is removed by a pressure swing adsorption unit. The tail gas from the pressure swing adsorption unit is further reformed with the addition of a hydrocarbon containing stream in a steam methane reforming system, further shifted to produce further additional hydrogen. The further hydrogen is then separated in another pressure swing adsorption unit.
摘要翻译： 一种氢气生产方法和设备，其中在合成气处理单元中处理通过碳质物质的气化产生的合成气流，其中一氧化碳含量与蒸汽反应以产生通过变压吸附除去的附加氢 单元。 来自变压吸附单元的尾气通过在蒸汽甲烷重整系统中加入含烃流进一步重整，进一步转移以产生另外的氢。 然后在另一个变压吸附单元中分离另外的氢。
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公开(公告)号：US5582036A
公开(公告)日：1996-12-10
申请号：US521497
申请日：1995-08-30
CPC分类号： F25J3/04418 , F25J3/0409 , F25J3/04303 , F25J3/04557 , F25J3/046 , F25J2200/34 , F25J2200/54 , F25J2215/02 , F25J2215/52 , F25J2245/50 , Y10S62/915
摘要： A system which integrates a cryogenic air separation plant with a blast furnace system enabling efficient oxygen enrichment of the blast air, and, if desired, production of additional higher purity oxygen.
摘要翻译： 将低温空气分离装置与高炉系统相集成的系统，其能够高效地富集鼓风空气，并且如果需要，可生产额外的较高纯度的氧气。
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