RU98108324A - METHOD FOR SEPARATING OXYGEN GAS FLOW TO OXYGEN ENRICHED GAS FLOW AND OXYGEN DECIDED GAS FLOW (OPTIONS) - Google Patents

METHOD FOR SEPARATING OXYGEN GAS FLOW TO OXYGEN ENRICHED GAS FLOW AND OXYGEN DECIDED GAS FLOW (OPTIONS)

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Publication number
RU98108324A
RU98108324A RU98108324/12A RU98108324A RU98108324A RU 98108324 A RU98108324 A RU 98108324A RU 98108324/12 A RU98108324/12 A RU 98108324/12A RU 98108324 A RU98108324 A RU 98108324A RU 98108324 A RU98108324 A RU 98108324A
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RU
Russia
Prior art keywords
gas stream
oxygen
membrane
section
ion transfer
Prior art date
Application number
RU98108324/12A
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Russian (ru)
Other versions
RU2182036C2 (en
Inventor
Фридрих Готтзманн Кристиан
Прасад Рави
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Праксайр Текнолоджи, Инк.
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Priority claimed from US08/848,199 external-priority patent/US5820654A/en
Application filed by Праксайр Текнолоджи, Инк. filed Critical Праксайр Текнолоджи, Инк.
Publication of RU98108324A publication Critical patent/RU98108324A/en
Application granted granted Critical
Publication of RU2182036C2 publication Critical patent/RU2182036C2/en

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Claims (10)

1. Способ разделения кислородного газового потока на обогащенный кислородом газовый поток и обедненный кислородом газовый поток посредством предварительного выделения кислорода из подаваемого газового потока, содержащего элементарный кислород и последующего охлаждения, получаемого из него кислородного газового потока или обогащенного кислородом газового потока, в одном устройстве, имеющем секцию разделения и секцию охлаждения и вывода для кислородного продукта, в котором секция разделения включает в себя мембрану для переноса ионов, имеющую сторону подвода и сторону отвода, причем способ содержит следующие операции: сжатие подаваемого газового потока, разделение сжатого подаваемого газового потока на основную часть газового потока и вспомогательную часть газового потока, нагрев основной части газового потока, введение нагретой основной части газового потока в секцию разделения устройства, введение вспомогательной части газового потока в секцию охлаждения устройства рядом с выходом для кислородного продукта, отвод кислорода из нагретой основной части газового потока через мембрану для переноса ионов в секции разделения с целью получения горячего обогащенного кислородом газового потока на стороне отвода от мембраны и обедненного кислородом газового потока на стороне подвода к мембране, и передачу тепла от обогащенного кислородом газового потока вспомогательной части газового потока с целью получения кислородного газового потока или газового потока, обогащенного кислородом продукта и нагретой вспомогательной части газового потока, причем вспомогательную часть газового потока либо выводят из устройства, либо объединяют с нагретой основной частью газового потока перед вводом нагретой основной части газового потока в секцию разделения и в котором обедненный кислородом газовый поток выводят из устройства.1. A method for separating an oxygen gas stream into an oxygen-enriched gas stream and an oxygen-depleted gas stream by pre-separating oxygen from a supplied gas stream containing elemental oxygen and then cooling the oxygen gas stream or oxygen-enriched gas stream obtained therefrom in one device having a separation section and a cooling and outlet section for an oxygen product, in which the separation section includes an ion transfer membrane in, having a supply side and a discharge side, the method comprising the following operations: compressing the supplied gas stream, separating the compressed supplied gas stream into the main part of the gas stream and the auxiliary part of the gas stream, heating the main part of the gas stream, introducing the heated main part of the gas stream into the section separation of the device, the introduction of the auxiliary part of the gas stream into the cooling section of the device near the outlet for the oxygen product, the removal of oxygen from the heated main part of the gas flow through the membrane for ion transfer to the separation section in order to obtain a hot oxygen-enriched gas stream on the outlet side from the membrane and an oxygen-depleted gas stream on the supply side to the membrane, and heat transfer from the oxygen-enriched gas stream to the auxiliary part of the gas stream to produce oxygen gas a stream or a gas stream enriched with oxygen of the product and a heated auxiliary part of the gas stream, wherein the auxiliary part of the gas stream or an outlet t from the device, or combined with the main part of the heated gas stream prior to entering the main part of the heated gas stream into the separation zone and wherein oxygen-depleted gas stream is withdrawn from the device. 2. Способ по п.1, в котором устройство дополнительно содержит секцию реактора, включающую в себя мембрану для переноса ионов, имеющую сторону подвода и сторону отвода и в котором химически активный газовый поток вводят на стороне отвода от мембраны для переноса ионов в секции реактора устройства для вступления в реакцию со вторым кислородным газовым потоком, проникающим через мембрану для переноса ионов рядом со стороной отвода от мембраны для переноса ионов для получения газового потока продуктов реакции, который используется для продувки стороны отвода от мембраны для переноса ионов в секции разделения устройства, и в котором газовый поток продуктов реакции и первый кислородный газовый поток и любой, не вступивший в реакцию кислород из второго кислородного газового потока объединяют в виде обогащенного кислородом газового потока, который выходит из устройства и в котором обедненный кислородом газовый поток отдельно выводят из устройства. 2. The method according to claim 1, in which the device further comprises a reactor section including an ion transfer membrane having a supply side and a discharge side and in which a reactive gas stream is introduced on the discharge side of the ion transfer membrane into the reactor section of the device for reacting with a second oxygen gas stream penetrating through the ion transfer membrane adjacent to the outlet side of the ion transfer membrane to produce a gas stream of reaction products that is used to purge the sides of the outlet side from the ion transfer membrane to the separation section of the device, and in which the gas stream of the reaction products and the first oxygen gas stream and any unreacted oxygen from the second oxygen gas stream are combined in the form of an oxygen-enriched gas stream that exits the device and in which the oxygen-depleted gas stream is separately removed from the device. 3. Способ по п.2, в котором мембрана для переноса ионов секции разделения устройства и мембрана для переноса ионов секции реактора устройства образованы совместно. 3. The method according to claim 2, in which the membrane for ion transfer of the separation section of the device and the membrane for ion transfer of the reactor section of the device are formed together. 4. Способ по п.3, в котором мембрана для переноса ионов секции разделения устройства включает в себя пористую поддерживающую подложку и содержит материал для переноса ионов, имеющий высокую проводимость кислорода при высоком парциальном давлении кислорода, а мембрана для переноса ионов секции реактора устройства содержит слой смешанного проводника, имеющего оптимальную стойкость при низком парциальном давлении кислорода. 4. The method according to claim 3, in which the membrane for ion transfer of the separation section of the device includes a porous support substrate and contains material for ion transfer having high oxygen conductivity at a high oxygen partial pressure, and the membrane for ion transfer of the reactor section of the device contains a layer mixed conductor having optimal resistance at low oxygen partial pressure. 5. Способ по п.3, в котором мембрана для переноса ионов секции реактора и мембрана для переноса ионов секции разделения образованы совместно с трубопроводом для переноса обогащенного кислородом газового потока через секцию охладителя устройства. 5. The method according to claim 3, in which the membrane for ion transfer of the reactor section and the membrane for ion transfer of the separation section are formed in conjunction with a pipeline for transferring oxygen-enriched gas stream through the cooler section of the device. 6. Способ по п.5, в котором трубопровод для перенесения обогащенного кислородом газового потока через секцию охлаждения представляет собой металлическую трубу и соединяется с мембраной для переноса ионов секции реактора устройства посредством сварки или пайки твердым припоем. 6. The method according to claim 5, in which the pipeline for transferring the oxygen-rich gas stream through the cooling section is a metal pipe and is connected to the membrane for transferring ions of the reactor section of the device by welding or brazing. 7. Способ по п.5, в котором трубопровод для переноса обогащенного кислородом газового потока через секцию охлаждения устройства содержит плотный уплотняющий материал и соединяется с мембраной для переноса ионов секции реактора устройства посредством сварки или пайки твердым припоем. 7. The method according to claim 5, in which the pipeline for transferring the oxygen-rich gas stream through the cooling section of the device contains a dense sealing material and is connected to the membrane for transferring ions of the reactor section of the device by welding or brazing. 8. Способ по п.2, в котором химически активный газ нагревают перед его вводом в секцию реактора устройства. 8. The method according to claim 2, in which the reactive gas is heated before it is introduced into the reactor section of the device. 9. Способ по п. 1, в котором секция разделения включает в себя секцию реактора, а операция отвода кислорода через мембрану включает в себя введение химически активного газового потока на стороне отвода от мембраны для переноса ионов для вступления в реакцию, по меньшей мере, с частью переносимого кислорода. 9. The method according to p. 1, in which the separation section includes a reactor section, and the operation of removing oxygen through the membrane includes the introduction of a reactive gas stream on the side of the outlet from the membrane to transfer ions to enter into reaction, at least part of the oxygen transported. 10. Способ разделения газового потока на обогащенный кислородом газовый поток и обедненный кислородом газовый поток посредством выделения кислорода из подаваемого газового потока, содержащего элементарный кислород, в устройстве, имеющем секцию реактора и секцию разделения, в котором каждая из секций реактора и разделения включает в себя, по меньшей мере, одну мембрану для переноса ионов, имеющую сторону подвода и сторону отвода, причем способ содержит следующие операции: сжатие подаваемого газового потока, введение сжатого подаваемого газового потока в устройство и передачу тепла от газового потока продуктов реакции передаваемому газовому потоку, отвод кислорода из нагретого подаваемого газового потока посредством пропускания через мембрану для переноса ионов в секции реактора с целью получения газового потока продуктов реакции на стороне отвода от мембраны и частично обедненного кислородом газового потока на стороне подвода к мембране, удаление дополнительного кислорода из частично обедненного кислородом газового потока с помощью мембраны для переноса ионов в секции разделения с целью получения обедненного кислородом газового потока на стороне подачи к мембране, в котором химически активный газовый поток вводят на стороне отвода от мембраны для переноса ионов в секции реактора для вступления в реакцию с кислородом, пропускаемым через мембрану для переноса ионов, рядом со стороной отвода от мембраны для получения газового потока продуктов реакции, используемого для продувки стороны отвода от мембраны для переноса ионов в секции разделения, и в котором газовый поток продуктов реакции и не вступивший в реакцию кислород объединяются в виде обогащенного кислородом газового потока, выпускаемого из устройства и в котором обедненный кислородом газовый поток отдельно выводят из устройства. 10. A method of separating a gas stream into an oxygen-enriched gas stream and an oxygen-depleted gas stream by separating oxygen from a supplied gas stream containing elemental oxygen in a device having a reactor section and a separation section in which each of the reactor and separation sections includes, at least one ion transfer membrane having an inlet side and an outlet side, the method comprising the following operations: compressing the feed gas stream, introducing the compressed feed the gas flow to the device and heat transfer from the gas stream of the reaction products to the transmitted gas stream, the removal of oxygen from the heated feed gas stream by passing through the membrane to transfer ions into the reactor sections in order to obtain a gas stream of reaction products on the outlet side from the membrane and partially oxygen-depleted gas flow on the supply side to the membrane, removal of additional oxygen from the gas stream partially depleted of oxygen using a membrane for ion transfer to separation section in order to obtain an oxygen-depleted gas stream on the supply side to the membrane, in which a reactive gas stream is introduced on the discharge side of the ion transfer membrane into the reactor sections to react with oxygen passing through the ion transfer membrane near the side the outlet from the membrane to obtain a gas stream of reaction products used to purge the side of the outlet from the membrane to transfer ions into the separation section, and in which the gas stream of the reaction products does not rise ivshy reacted oxygen are combined in the form of oxygen-enriched gas stream discharged from the unit, and wherein oxygen-depleted gas stream separately output from the apparatus.
RU98108324/12A 1997-04-29 1998-04-28 METHOD OF SEPARATION OF OXYGEN GAS FLOW INTO GAS FLOW ENRICHED IN OXYGEN AND GAS FLOW DEPLETED IN OXYGEN (Versions) RU2182036C2 (en)

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US08/848,199 US5820654A (en) 1997-04-29 1997-04-29 Integrated solid electrolyte ionic conductor separator-cooler
US08/848,199 1997-04-29

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2447928C1 (en) * 2010-11-18 2012-04-20 Закрытое Акционерное Общество "Грасис" Method of separating and cleaning gas mixes to parameters of consumption

Families Citing this family (76)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5820654A (en) * 1997-04-29 1998-10-13 Praxair Technology, Inc. Integrated solid electrolyte ionic conductor separator-cooler
US5954859A (en) * 1997-11-18 1999-09-21 Praxair Technology, Inc. Solid electrolyte ionic conductor oxygen production with power generation
US6056807A (en) * 1998-01-26 2000-05-02 Air Products And Chemicals, Inc. Fluid separation devices capable of operating under high carbon dioxide partial pressures which utilize creep-resistant solid-state membranes formed from a mixed conducting multicomponent metallic oxide
US6010614A (en) * 1998-06-03 2000-01-04 Praxair Technology, Inc. Temperature control in a ceramic membrane reactor
US6139810A (en) * 1998-06-03 2000-10-31 Praxair Technology, Inc. Tube and shell reactor with oxygen selective ion transport ceramic reaction tubes
US6017646A (en) * 1998-06-03 2000-01-25 Praxair Technology, Inc. Process integrating a solid oxide fuel cell and an ion transport reactor
US6296687B2 (en) * 1999-04-30 2001-10-02 Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of Natural Resources Hydrogen permeation through mixed protonic-electronic conducting materials
US6521202B1 (en) 1999-06-28 2003-02-18 University Of Chicago Oxygen ion conducting materials
US6302402B1 (en) 1999-07-07 2001-10-16 Air Products And Chemicals, Inc. Compliant high temperature seals for dissimilar materials
NO313493B1 (en) * 1999-09-28 2002-10-14 Norsk Hydro As Solid multicomponent membrane comprising a mixed metal oxide for use in a heat or synthesis gas reactor
US6454274B2 (en) 2000-03-27 2002-09-24 Praxair Technology, Inc. Joint assembly for joining a ceramic membrane to a tube sheet
US6293084B1 (en) 2000-05-04 2001-09-25 Praxair Technology, Inc. Oxygen separator designed to be integrated with a gas turbine and method of separating oxygen
CA2422667C (en) * 2000-09-08 2007-01-30 Nippon Steel Corporation Ceramic-metal composite body, composite structure for transporting oxide ion, and composite body having sealing property
CA2422567A1 (en) 2000-09-20 2003-03-18 Hideki Kurimura Method for partial oxidation of methane using dense, oxygen selective permeation ceramic membrane
FR2817860B1 (en) * 2000-12-07 2003-09-12 Air Liquide PROCESS FOR THE PREPARATION OF A LOW THICKNESS CERAMIC MATERIAL WITH CONTROLLED SURFACE POROSITY GRADIENT, CERAMIC MATERIAL OBTAINED, ELECTROCHEMICAL CELL AND CERAMIC MEMBRANE COMPRISING THE SAME
US6562104B2 (en) * 2000-12-19 2003-05-13 Praxair Technology, Inc. Method and system for combusting a fuel
DE10064894A1 (en) * 2000-12-23 2002-06-27 Alstom Switzerland Ltd Air decomposition device, used in power stations, comprises housing separated into chambers by membrane body
FR2826956B1 (en) * 2001-07-04 2004-05-28 Air Liquide PROCESS FOR PREPARING A LOW THICKNESS CERAMIC COMPOSITION WITH TWO MATERIALS, COMPOSITION OBTAINED, ELECTROCHEMICAL CELL AND MEMBRANE COMPRISING IT
WO2003009811A2 (en) * 2001-07-25 2003-02-06 Haase Richard A Processes and apparatus for the manufacture of polynuclear aluminum compounds and disinfectants, and polynuclear aluminum compounds and disinfectants from such processes and apparatus
US20030039601A1 (en) * 2001-08-10 2003-02-27 Halvorson Thomas Gilbert Oxygen ion transport membrane apparatus and process for use in syngas production
US6709782B2 (en) * 2001-10-01 2004-03-23 Delphi Technologies, Inc. Fuel cell having an anode protected from high oxygen ion concentration
US6565632B1 (en) * 2001-12-17 2003-05-20 Praxair Technology, Inc. Ion-transport membrane assembly incorporating internal support
CA2482454C (en) * 2002-04-11 2011-12-20 Richard A. Haase Water combustion technology-methods, processes, systems and apparatus for the combustion of hydrogen and oxygen
US6702570B2 (en) * 2002-06-28 2004-03-09 Praxair Technology Inc. Firing method for a heat consuming device utilizing oxy-fuel combustion
US7252810B2 (en) * 2002-07-12 2007-08-07 Parsa Investments, L.P. Multi-sectional system for continuous gas separation
US7226679B2 (en) * 2002-07-31 2007-06-05 Siemens Power Generation, Inc. Fuel cell system with degradation protected anode
US7314502B2 (en) * 2002-09-25 2008-01-01 Exxonmobil Upstream Research Company Method and system for separating a component from a multi-component gas
WO2004060539A1 (en) * 2002-12-19 2004-07-22 Exxonmobil Upstream Research Company Membrane module for separation of fluids
US7425231B2 (en) * 2003-08-06 2008-09-16 Air Products And Chemicals, Inc. Feed gas contaminant removal in ion transport membrane systems
US7658788B2 (en) * 2003-08-06 2010-02-09 Air Products And Chemicals, Inc. Ion transport membrane module and vessel system with directed internal gas flow
US7179323B2 (en) * 2003-08-06 2007-02-20 Air Products And Chemicals, Inc. Ion transport membrane module and vessel system
US7771519B2 (en) * 2005-01-03 2010-08-10 Air Products And Chemicals, Inc. Liners for ion transport membrane systems
US8268269B2 (en) 2006-01-24 2012-09-18 Clearvalue Technologies, Inc. Manufacture of water chemistries
JP5205910B2 (en) * 2006-10-31 2013-06-05 三菱マテリアル株式会社 Trichlorosilane production equipment
US7856829B2 (en) * 2006-12-15 2010-12-28 Praxair Technology, Inc. Electrical power generation method
US7771509B1 (en) * 2007-09-07 2010-08-10 Cryogenic Group, Inc. Magnetic oxygen concentrator for air streams
US8500872B2 (en) * 2008-01-02 2013-08-06 Technion Research & Development Foundation Ltd. Ceramic tubes composed of two materials
KR101579308B1 (en) * 2008-02-25 2015-12-21 가부시키가이샤 노리타케 캄파니 리미티드 Ceramic product and ceramic member bonding method
US8465630B2 (en) * 2008-11-10 2013-06-18 Praxair Technology, Inc. Oxygen separation assembly and method
JP2012011880A (en) * 2010-06-30 2012-01-19 Denso Corp Air filter device
US9417013B2 (en) * 2010-11-12 2016-08-16 Toyota Motor Engineering & Manufacturing North America, Inc. Heat transfer systems including heat conducting composite materials
US9561476B2 (en) 2010-12-15 2017-02-07 Praxair Technology, Inc. Catalyst containing oxygen transport membrane
US8435332B2 (en) * 2011-04-08 2013-05-07 Praxair Technology, Inc. Oxygen separation module and apparatus
US9486735B2 (en) 2011-12-15 2016-11-08 Praxair Technology, Inc. Composite oxygen transport membrane
EP2791082B1 (en) * 2011-12-15 2021-01-20 Praxair Technology, Inc. Method of producing composite oxygen transport membrane
WO2014100376A1 (en) 2012-12-19 2014-06-26 Praxair Technology, Inc. Method for sealing an oxygen transport membrane assembly
US9453644B2 (en) 2012-12-28 2016-09-27 Praxair Technology, Inc. Oxygen transport membrane based advanced power cycle with low pressure synthesis gas slip stream
DE102013103426B4 (en) * 2013-04-05 2018-01-04 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Process and membrane module for energy-efficient oxygen production in biomass gasification
US9296671B2 (en) 2013-04-26 2016-03-29 Praxair Technology, Inc. Method and system for producing methanol using an integrated oxygen transport membrane based reforming system
US9611144B2 (en) 2013-04-26 2017-04-04 Praxair Technology, Inc. Method and system for producing a synthesis gas in an oxygen transport membrane based reforming system that is free of metal dusting corrosion
US9938145B2 (en) 2013-04-26 2018-04-10 Praxair Technology, Inc. Method and system for adjusting synthesis gas module in an oxygen transport membrane based reforming system
US9212113B2 (en) 2013-04-26 2015-12-15 Praxair Technology, Inc. Method and system for producing a synthesis gas using an oxygen transport membrane based reforming system with secondary reforming and auxiliary heat source
WO2015054228A2 (en) 2013-10-07 2015-04-16 Praxair Technology, Inc. Ceramic oxygen transport membrane array reactor and reforming method
CA2924201A1 (en) * 2013-10-08 2015-04-16 Praxair Technology, Inc. System and method for temperature control in an oxygen transport membrane based reactor
CN105764842B (en) 2013-12-02 2018-06-05 普莱克斯技术有限公司 Use the method and system of the production hydrogen of the reforming system based on oxygen transport film with two process transform
US9383096B2 (en) 2013-12-23 2016-07-05 King Fahd University Of Petroleum And Minerals Carbon-free low-NOx liquid fuel oxygen transport reactor for industrial water tube boilers
WO2015123246A2 (en) 2014-02-12 2015-08-20 Praxair Technology, Inc. Oxygen transport membrane reactor based method and system for generating electric power
WO2015160609A1 (en) 2014-04-16 2015-10-22 Praxair Technology, Inc. Method and system for oxygen transport membrane enhanced integrated gasifier combined cycle (igcc)
US10006369B2 (en) 2014-06-30 2018-06-26 General Electric Company Method and system for radial tubular duct heat exchangers
US9789445B2 (en) 2014-10-07 2017-10-17 Praxair Technology, Inc. Composite oxygen ion transport membrane
US9835380B2 (en) * 2015-03-13 2017-12-05 General Electric Company Tube in cross-flow conduit heat exchanger
US10441922B2 (en) 2015-06-29 2019-10-15 Praxair Technology, Inc. Dual function composite oxygen transport membrane
US10118823B2 (en) 2015-12-15 2018-11-06 Praxair Technology, Inc. Method of thermally-stabilizing an oxygen transport membrane-based reforming system
US9938146B2 (en) 2015-12-28 2018-04-10 Praxair Technology, Inc. High aspect ratio catalytic reactor and catalyst inserts therefor
US10378835B2 (en) 2016-03-25 2019-08-13 Unison Industries, Llc Heat exchanger with non-orthogonal perforations
US10202946B2 (en) * 2016-03-29 2019-02-12 King Fahd University Of Petroleum And Minerals Power turbine system
EP3436185A1 (en) 2016-04-01 2019-02-06 Praxair Technology Inc. Catalyst-containing oxygen transport membrane
EA036885B1 (en) * 2016-08-31 2021-01-11 8 Риверз Кэпитл, Ллк System and method for power production utilizing ion transport devices
US10018352B1 (en) * 2017-04-21 2018-07-10 King Fahd University Of Petroleum And Minerals Fire tube boiler system with ion transport membranes
US10711937B2 (en) 2017-05-25 2020-07-14 Fisher Controls International Llc Method of manufacturing a fluid pressure reduction device
US10697561B2 (en) * 2017-05-25 2020-06-30 Fisher Controls International Llc Method of manufacturing a fluid pressure reduction device
US11136238B2 (en) 2018-05-21 2021-10-05 Praxair Technology, Inc. OTM syngas panel with gas heated reformer
WO2020117580A1 (en) * 2018-12-03 2020-06-11 Carrier Corporation Membrane purge system
CN112334721A (en) 2018-12-03 2021-02-05 开利公司 Enhanced refrigeration purge system
US11913693B2 (en) 2018-12-03 2024-02-27 Carrier Corporation Enhanced refrigeration purge system
US11773497B2 (en) 2020-03-04 2023-10-03 Massachusetts Institute Of Technology Combined cycle power system

Family Cites Families (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1685759A (en) * 1924-05-22 1928-09-25 Ver Fur Chemische Ind Ag Diffusion reaction
US3550355A (en) * 1967-12-22 1970-12-29 Gen Am Transport Oxygen separation process
US3847672A (en) * 1971-08-18 1974-11-12 United Aircraft Corp Fuel cell with gas separator
US3849076A (en) * 1972-06-21 1974-11-19 V Gryaznov Catalytic reactor for carrying out conjugate chemical reactions
US3901669A (en) * 1973-11-05 1975-08-26 Sun Ventures Inc Manufacture of hydrogen from high temperature steam
SU573444A1 (en) * 1974-06-11 1977-09-25 Новомосковский Химический Комбинат Им. В.И.Ленина Apparatus for separating hydrogen from gas mixture
FR2366217A1 (en) * 1975-08-27 1978-04-28 Comp Generale Electricite HYDROGEN GENERATOR DEVICE
CA1213128A (en) * 1982-10-07 1986-10-28 Arie L. Mos Reactor for exothermic or endothermic chemical processes
SU1472104A1 (en) * 1986-09-23 1989-04-15 Предприятие П/Я А-1157 Membrane apparatus for extracting hydrogen from gas mixtures
US5306411A (en) * 1989-05-25 1994-04-26 The Standard Oil Company Solid multi-component membranes, electrochemical reactor components, electrochemical reactors and use of membranes, reactor components, and reactor for oxidation reactions
EP0462226B1 (en) * 1989-03-08 1995-05-10 Rocky Research Method and apparatus for achieving high reaction rates in solid-gas reactor systems
DE3921390A1 (en) * 1989-06-29 1991-01-17 Merck Patent Gmbh METHOD AND DEVICE FOR PRODUCING PURE OXYGEN
US5342431A (en) * 1989-10-23 1994-08-30 Wisconsin Alumni Research Foundation Metal oxide membranes for gas separation
US5229102A (en) * 1989-11-13 1993-07-20 Medalert, Inc. Catalytic ceramic membrane steam-hydrocarbon reformer
US5169415A (en) * 1990-08-31 1992-12-08 Sundstrand Corporation Method of generating oxygen from an air stream
US5160713A (en) * 1990-10-09 1992-11-03 The Standard Oil Company Process for separating oxygen from an oxygen-containing gas by using a bi-containing mixed metal oxide membrane
US5186793A (en) * 1990-12-31 1993-02-16 Invacare Corporation Oxygen concentrator utilizing electrochemical cell
GB2257054A (en) * 1991-07-04 1993-01-06 Normalair Garrett Oxygen generating system
US5240473A (en) * 1992-09-01 1993-08-31 Air Products And Chemicals, Inc. Process for restoring permeance of an oxygen-permeable ion transport membrane utilized to recover oxygen from an oxygen-containing gaseous mixture
US5240480A (en) * 1992-09-15 1993-08-31 Air Products And Chemicals, Inc. Composite mixed conductor membranes for producing oxygen
JPH06134244A (en) * 1992-10-20 1994-05-17 Orion Mach Co Ltd Membrane gas drier
US5384051A (en) * 1993-02-05 1995-01-24 Mcginness; Thomas G. Supercritical oxidation reactor
US5565017A (en) * 1993-12-17 1996-10-15 Air Products And Chemicals, Inc. High temperature oxygen production with steam and power generation
US5516359A (en) * 1993-12-17 1996-05-14 Air Products And Chemicals, Inc. Integrated high temperature method for oxygen production
US5447555A (en) * 1994-01-12 1995-09-05 Air Products And Chemicals, Inc. Oxygen production by staged mixed conductor membranes
JP3402515B2 (en) * 1994-05-23 2003-05-06 日本碍子株式会社 Hydrogen separator, hydrogen separator using the same, and method for producing hydrogen separator
US5552039A (en) * 1994-07-13 1996-09-03 Rpc Waste Management Services, Inc. Turbulent flow cold-wall reactor
US5480620A (en) * 1994-08-17 1996-01-02 Cameron; Gordon M. Catalytic converter
AU706663B2 (en) * 1994-09-23 1999-06-17 Standard Oil Company, The Oxygen permeable mixed conductor membranes
US5681373A (en) * 1995-03-13 1997-10-28 Air Products And Chemicals, Inc. Planar solid-state membrane module
US5599383A (en) * 1995-03-13 1997-02-04 Air Products And Chemicals, Inc. Tubular solid-state membrane module
US5547494A (en) * 1995-03-22 1996-08-20 Praxair Technology, Inc. Staged electrolyte membrane
DE69619299T2 (en) * 1995-06-07 2002-10-10 Air Prod & Chem Oxygen production with ion transport membranes and energy recovery
US5611931A (en) * 1995-07-31 1997-03-18 Media And Process Technology Inc. High temperature fluid separations using ceramic membrane device
US5837125A (en) * 1995-12-05 1998-11-17 Praxair Technology, Inc. Reactive purge for solid electrolyte membrane gas separation
US5820654A (en) * 1997-04-29 1998-10-13 Praxair Technology, Inc. Integrated solid electrolyte ionic conductor separator-cooler

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2447928C1 (en) * 2010-11-18 2012-04-20 Закрытое Акционерное Общество "Грасис" Method of separating and cleaning gas mixes to parameters of consumption

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