BR0212821A - Método combinado de separação de oxigênio de um gás contendo oxigênio e geração de energia - Google Patents

Método combinado de separação de oxigênio de um gás contendo oxigênio e geração de energia

Info

Publication number
BR0212821A
BR0212821A BR0212821-7A BR0212821A BR0212821A BR 0212821 A BR0212821 A BR 0212821A BR 0212821 A BR0212821 A BR 0212821A BR 0212821 A BR0212821 A BR 0212821A
Authority
BR
Brazil
Prior art keywords
oxygen
pressurized
stream
product
power generation
Prior art date
Application number
BR0212821-7A
Other languages
English (en)
Inventor
Christian Friedrich Gottzmann
Original Assignee
Praxair Technology Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Praxair Technology Inc filed Critical Praxair Technology Inc
Publication of BR0212821A publication Critical patent/BR0212821A/pt

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06—Tubular membrane modules
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08—Flat membrane modules
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0229—Purification or separation processes
    • C01B13/0248—Physical processing only
    • C01B13/0251—Physical processing only by making use of membranes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K3/00—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
    • F01K3/18—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters
    • F01K3/185—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters using waste heat from outside the plant
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/22—Cooling or heating elements
    • B01D2313/221—Heat exchangers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/42—Catalysts within the flow path
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2210/00—Purification or separation of specific gases
    • C01B2210/0043—Impurity removed
    • C01B2210/0046—Nitrogen
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2210/00—Purification or separation of specific gases
    • C01B2210/0043—Impurity removed
    • C01B2210/0062—Water
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

"MéTODO COMBINADO DE SEPARAçãO DE OXIGêNIO DE UM GáS CONTENDO OXIGêNIO E GERAçãO DE ENERGIA". Um método de separação de oxigênio e para a geração de energia combinadas. Uma corrente contendo oxigênio é comprimida e oxigênio é separado da corrente em oxigênio permeado e um retido empobrecido em oxigênio em uma unidade de membranas transportadoras de oxigênio (25). Um lado de anodo (26) da unidade de membranas transportadoras de oxigênio (25) é purgado com uma corrente de purga pressurizada (42; 42b) composta de vapor d'água superaquecido, pressurizado. Uma corrente de produto de oxigênio pressurizado (20; 20a) é descarregada do lado de anodo (26) da membrana transportadora de oxigênio (25), o produto compreendendo vapor d'água e oxigênio permeado. A corrente de produto de oxigênio pressurizado (20; 20a) é esfriada contra si mesma ou a corrente contendo oxigênio. A corrente de produto de oxigênio pressurizado (20; 20a) é condensada por transferência de calor indireta com um fluido de processo (46) que ebule para permitir que energia seja extraída do fluido de processo. água condensada (56) é separada da corrente de produto de oxigênio (20; 20a) e oxigênio separado é extraído como um produto (3; 3a) sob pressão.
BR0212821-7A 2001-09-27 2002-09-24 Método combinado de separação de oxigênio de um gás contendo oxigênio e geração de energia BR0212821A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/963,492 US6562105B2 (en) 2001-09-27 2001-09-27 Combined method of separating oxygen and generating power
PCT/US2002/030190 WO2003035223A1 (en) 2001-09-27 2002-09-24 Combined oxygen separation and power generation method

Publications (1)

Publication Number Publication Date
BR0212821A true BR0212821A (pt) 2004-10-13

Family

ID=25507320

Family Applications (1)

Application Number Title Priority Date Filing Date
BR0212821-7A BR0212821A (pt) 2001-09-27 2002-09-24 Método combinado de separação de oxigênio de um gás contendo oxigênio e geração de energia

Country Status (7)

Country Link
US (1) US6562105B2 (pt)
EP (1) EP1432496A1 (pt)
JP (1) JP2005507041A (pt)
CN (1) CN1592649A (pt)
BR (1) BR0212821A (pt)
CA (1) CA2461604A1 (pt)
WO (1) WO2003035223A1 (pt)

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US7967878B2 (en) 2002-01-04 2011-06-28 Meggitt (Uk) Limited Reformer apparatus and method
US8177868B2 (en) 2002-01-04 2012-05-15 Meggitt (Uk) Limited Reforming apparatus and method
US6913636B2 (en) * 2002-12-17 2005-07-05 Hamilton Sundstrand Corporation Low power nitrogen enriched air generation system
US7122072B2 (en) * 2003-11-17 2006-10-17 Air Products And Chemicals, Inc. Controlled heating and cooling of mixed conducting metal oxide materials
US7118612B2 (en) * 2003-12-30 2006-10-10 Praxair Technology, Inc. Oxygen separation method utilizing an oxygen transport membrane reactor
US20100071381A1 (en) * 2006-07-28 2010-03-25 Rollins Iii William S High efficiency integrated gasification combined cycle power plant
DE102006035790B3 (de) * 2006-07-28 2008-03-27 Siemens Ag Verfahren zum Betrieb einer Kraftwerksanlage mit integrierter Kohlevergasung sowie Kraftwerksanlage
US7947115B2 (en) * 2006-11-16 2011-05-24 Siemens Energy, Inc. System and method for generation of high pressure air in an integrated gasification combined cycle system
EP2026004A1 (de) * 2007-08-07 2009-02-18 Siemens Aktiengesellschaft Verfahren zum Betrieb einer Verbrennungsanlage sowie Verbrennungsanlage
US7771509B1 (en) * 2007-09-07 2010-08-10 Cryogenic Group, Inc. Magnetic oxygen concentrator for air streams
US7954458B2 (en) * 2007-11-14 2011-06-07 Alstom Technology Ltd Boiler having an integrated oxygen producing device
FR2924755B1 (fr) * 2007-12-05 2014-06-13 Air Liquide Cycle combine a reacteur ceramique membranaire d'oxycombustion refroidi a l'eau.
US20120023947A1 (en) * 2010-07-30 2012-02-02 General Electric Company Systems and methods for co2 capture
WO2012085860A1 (en) * 2010-12-21 2012-06-28 Inbicon A/S Steam delivery system for biomass processing
US20140004470A1 (en) * 2012-06-29 2014-01-02 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method and System for Injecting Low Pressure Oxygen from an Ion Transport Membrane into an Ambient or Super Ambient Pressure Oxygen-Consuming Process
DE102013202713A1 (de) 2013-02-20 2014-08-21 Technische Universität Dresden Vergasungsverfahren zur Erzeugung von Synthesegas mit integrierter Bereitstellung des Vergasungsmittels
EP2961684A2 (en) * 2013-02-28 2016-01-06 Air Products and Chemicals, Inc. Process and apparatus for producing oxygen and nitrogen using ion transport membranes
DE102014115849A1 (de) 2014-10-30 2016-05-04 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren und Anordnung zur Erzeugung und thermischen Kompression von Sauerstoff
EP3015660B1 (de) * 2014-10-31 2018-12-05 Orcan Energy AG Verfahren zum betreiben eines thermodynamischen kreisprozesses
DE102015119915A1 (de) * 2015-11-18 2017-05-18 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren und Vorrichtung zum Betrieb einer Gasturbine mit nasser Verbrennung
ES2770149B2 (es) * 2018-12-31 2023-02-23 Kerionics S L Procedimiento e instalación para la separación selectiva de gases en un proceso de oxicombustión mediante membranas permeables de oxígeno
US11491443B2 (en) * 2019-04-04 2022-11-08 Hamilton Sundstrand Corporation Process water gas management of electrochemical inert gas generating system

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US5565017A (en) * 1993-12-17 1996-10-15 Air Products And Chemicals, Inc. High temperature oxygen production with steam and power generation
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US5954859A (en) 1997-11-18 1999-09-21 Praxair Technology, Inc. Solid electrolyte ionic conductor oxygen production with power generation
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Also Published As

Publication number Publication date
EP1432496A1 (en) 2004-06-30
JP2005507041A (ja) 2005-03-10
CN1592649A (zh) 2005-03-09
CA2461604A1 (en) 2003-05-01
US6562105B2 (en) 2003-05-13
WO2003035223A1 (en) 2003-05-01
US20030056647A1 (en) 2003-03-27

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Legal Events

Date Code Title Description
B11A Dismissal acc. art.33 of ipl - examination not requested within 36 months of filing
B11Y Definitive dismissal - extension of time limit for request of examination expired [chapter 11.1.1 patent gazette]