KR910000216A - 공기 분리법 - Google Patents

공기 분리법 Download PDF

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KR910000216A
KR910000216A KR1019900008245A KR900008245A KR910000216A KR 910000216 A KR910000216 A KR 910000216A KR 1019900008245 A KR1019900008245 A KR 1019900008245A KR 900008245 A KR900008245 A KR 900008245A KR 910000216 A KR910000216 A KR 910000216A
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stream
fluid
nitrogen
oxygen
distillation column
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KR1019900008245A
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KR0163351B1 (ko
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라드본 토마스
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원본미기재
더 비오씨 그룹 피엘씨
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04539Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04248Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
    • F25J3/04284Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
    • F25J3/0429Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
    • F25J3/04303Lachmann expansion, i.e. expanded into oxygen producing or low pressure column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04406Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system
    • F25J3/04412Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04539Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels
    • F25J3/04545Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels for the gasification of solid or heavy liquid fuels, e.g. integrated gasification combined cycle [IGCC]
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04551Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the metal production
    • F25J3/04557Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the metal production for pig iron or steel making, e.g. blast furnace, Corex
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04563Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating
    • F25J3/04575Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating for a gas expansion plant, e.g. dilution of the combustion gas in a gas turbine
    • F25J3/04581Hot gas expansion of indirect heated nitrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04612Heat exchange integration with process streams, e.g. from the air gas consuming unit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/20Processes or apparatus using separation by rectification in an elevated pressure multiple column system wherein the lowest pressure column is at a pressure well above the minimum pressure needed to overcome pressure drop to reject the products to atmosphere

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

내용 없음

Description

공기 분리법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 결합된 공기분리 장치-화학 또는 금속학 장치-전력 발생기의 회로 배선도이며,
제2도는 제1도에 나타난 장치를 사용하기 위한 공기 분리 장치의 회로 배선도이다.

Claims (12)

  1. 2내지 7기압 범위의 절대압에서 질소 스트림을 유체의 상 변화 없이 초기에 600℃미만의 온도에서 유체의 스트림과 열 교환에 의해 가열시키고, 상기 가열된 질소 스트림을 터어빈에서 팽창시켜 외부 일을 수행하는, 공기를 산소화 질소로 분리시키는 방법.
  2. 제1항에 있어서, 상기 외부 일이 전기 발생인 방법.
  3. 제1항 또는 제2항에 있어서, 상기 유체 스트림의 온도가 초기에 200 내지 400℃범위인 방법.
  4. 제3항에 있어서, 상기 질소 스트림의 압력이 2 내지 5기압인 방법.
  5. 제1항 내지 제4항중 어느 한 항에 잇어서, 상기 유체스트림이 산업 공정으로부터 생성된 폐기 가스 스트림인 방법.
  6. 제5항에 있어서, 상기 산소를 상기 산업 공정에서 사용하는 방법.
  7. 제1항 내지 제4항중 어느 한 항에 있어서, 상기 유체 스트림이 상태 변화 없이 산업 공정으로부터 생성된 폐기 가스 스트림에 의해 가열된 열전달 오일인 방법.
  8. 제7항에 있어서, 상기 산소를 상기 산업 공정에서 사용하는 방법.
  9. 제1항 내지 제8항중 어느 한 항에 있어서, 상기 질소 스트림이 공기가 분리되는 증류 컬럼으로부터 직접 수득되어, 상기 증류 컬럼의 중간 위치에서 압축되지 않고 상기 유체 스트림과 열 교환하는 방법.
  10. 제9항에 있어서, 상기 질소 스트림이 상기 증류 컬럼의 중간 위치에서 대략 주위온도로 가온되어 상기 유체스트림과 열 교환하는 방법.
  11. 제9항 또는 제10항에 있어서, 상기 증류 컬럼이 이중 컬럼 배열중 보다 낮은 압력의 컬럼인 방법.
  12. 공기를 산소와 질소로 분리시키는 장치; 공기 분리 장치에 의해 생성된 질소 스트림을 2 내지 7기압 범위의 압력에서 유체의 상 변화없이 초기에 600℃미만의 온도에서 유체 스트림과 열 교환시키는 열 교환기; 및 상기 가열된 질소를 팽창시켜 외부 일을 수행하는 팽창 터어빈을 포함하는, 제1항에 청구된 방법을 수행하기 위한 장치.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019900008245A 1989-06-06 1990-06-05 공기 분리법 KR0163351B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB89130017 1989-06-06
GB8913001.7 1989-06-06
GB898913001A GB8913001D0 (en) 1989-06-06 1989-06-06 Air separation

Publications (2)

Publication Number Publication Date
KR910000216A true KR910000216A (ko) 1991-01-29
KR0163351B1 KR0163351B1 (ko) 1998-11-16

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ID=10657976

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Application Number Title Priority Date Filing Date
KR1019900008245A KR0163351B1 (ko) 1989-06-06 1990-06-05 공기 분리법

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Country Link
US (1) US5040370A (ko)
EP (1) EP0402045B1 (ko)
JP (1) JP3188446B2 (ko)
KR (1) KR0163351B1 (ko)
AT (1) ATE102335T1 (ko)
CA (1) CA2018238A1 (ko)
DE (1) DE69006921T2 (ko)
DK (1) DK0402045T3 (ko)
ES (1) ES2049925T3 (ko)
GB (1) GB8913001D0 (ko)

Families Citing this family (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9111157D0 (en) * 1991-05-23 1991-07-17 Boc Group Plc Fluid production method and apparatus
FR2690711B1 (fr) * 1992-04-29 1995-08-04 Lair Liquide Procede de mise en óoeuvre d'un groupe turbine a gaz et ensemble combine de production d'energie et d'au moins un gaz de l'air.
US5265424A (en) * 1992-08-03 1993-11-30 Thomas Merritt Advanced furnace boiler system in electric power plant
US5459994A (en) * 1993-05-28 1995-10-24 Praxair Technology, Inc. Gas turbine-air separation plant combination
US5467613A (en) * 1994-04-05 1995-11-21 Carrier Corporation Two phase flow turbine
DE4426744A1 (de) 1994-07-28 1996-02-01 Sekurit Saint Gobain Deutsch Höhenverstellbares Seitenfenster für Kraftfahrzeuge
US5669958A (en) * 1996-02-29 1997-09-23 Membrane Technology And Research, Inc. Methane/nitrogen separation process
GB9624819D0 (en) * 1996-11-28 1997-01-15 Air Prod & Chem Use of elevated pressure nitrogen streams to perform work
NO308400B1 (no) * 1997-06-06 2000-09-11 Norsk Hydro As Kraftgenereringsprosess omfattende en forbrenningsprosess
NO308399B1 (no) * 1997-06-06 2000-09-11 Norsk Hydro As Prosess for generering av kraft og/eller varme
US6116027A (en) * 1998-09-29 2000-09-12 Air Products And Chemicals, Inc. Supplemental air supply for an air separation system
US6161386A (en) * 1998-12-23 2000-12-19 Membrane Technology And Research, Inc. Power generation method including membrane separation
US6263659B1 (en) 1999-06-04 2001-07-24 Air Products And Chemicals, Inc. Air separation process integrated with gas turbine combustion engine driver
US6345493B1 (en) 1999-06-04 2002-02-12 Air Products And Chemicals, Inc. Air separation process and system with gas turbine drivers
US6256994B1 (en) 1999-06-04 2001-07-10 Air Products And Chemicals, Inc. Operation of an air separation process with a combustion engine for the production of atmospheric gas products and electric power
US6745573B2 (en) 2001-03-23 2004-06-08 American Air Liquide, Inc. Integrated air separation and power generation process
US6601391B2 (en) 2001-06-19 2003-08-05 Geosol, Inc. Heat recovery
US6619041B2 (en) 2001-06-29 2003-09-16 L'air Liquide - Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Steam generation apparatus and methods
US6568185B1 (en) 2001-12-03 2003-05-27 L'air Liquide Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Combination air separation and steam-generation processes and plants therefore
US7128005B2 (en) * 2003-11-07 2006-10-31 Carter Jr Greg Non-polluting high temperature combustion system
US8065879B2 (en) * 2007-07-19 2011-11-29 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Thermal integration of oxygen plants
WO2009075897A2 (en) * 2007-12-06 2009-06-18 Brigham Young University Methods and systems for generating power from a turbine using pressurized nitrogen
EP2090335B1 (en) * 2008-02-12 2016-05-04 Zodiac Aerotechnics Oxygen breathing device
EP2168635B1 (en) * 2008-09-26 2017-06-28 Zodiac Aerotechnics Oxygen breathing device with redundant signal transmission
US8261744B2 (en) 2008-09-26 2012-09-11 Intertechnique, S.A. Oxygen breathing device with redundant signal transmission
EP2351600B1 (en) * 2008-09-26 2017-06-28 Zodiac Aerotechnics Oxygen breathing device with redundant signal transmission
CN102392704A (zh) * 2011-06-22 2012-03-28 赵军政 纯氧火力发电机组
DE102011113262A1 (de) 2011-09-13 2013-03-14 Linde Aktiengesellschaft Verfahren und Vorrichtung zur Gewinnung von Drucksauerstoff durch Tieftemperaturzerlegung von Luft
CN102679388A (zh) * 2012-05-22 2012-09-19 赵军政 高效节能环保的纯氧火力发电机组
CN115750017B (zh) * 2022-11-30 2024-05-24 国家电投集团科学技术研究院有限公司 液态空气储能耦合制氨发电系统及方法

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB189827153A (en) * 1898-12-23 1899-11-18 Edgar Charles Thrupp Invention relating to the Use of Liquefied Air to Produce Compressed Air for Driving Engines on Motor Cars, Tram Cars, or other Locomotives.
GB189917692A (en) * 1899-09-01 1900-03-31 Celeste Joly Improved Means and Apparatus for the Manufacture of Volatile Liquids and the Production of Mechanical Energy.
DE1102122B (de) * 1959-12-09 1961-03-16 Elektrochemisches Kom Bitterfe Verfahren zur Herstellung von wasserfreiem, geschmolzenem Magnesiumchlorid
US3241327A (en) * 1963-12-18 1966-03-22 Fleur Corp Waste heat recovery in air fractionation
US3987632A (en) * 1970-02-27 1976-10-26 Pereda Eugene F Liquid air engine
IL36741A (en) * 1971-04-30 1974-11-29 Zakon T Method for the separation of gaseous mixtures with recuperation of mechanical energy and apparatus for carrying out this method
US3987633A (en) * 1974-04-19 1976-10-26 Ford Jr Sanders Pressurized gas operated engine
DE3408937A1 (de) * 1984-01-31 1985-08-08 BBC Aktiengesellschaft Brown, Boveri & Cie., Baden, Aargau Kombinierte gas-/dampf-kraftwerkanlage
DE3446715A1 (de) * 1984-12-21 1986-06-26 Krupp Koppers GmbH, 4300 Essen Verfahren zur kuehlung von staubfoermige verunreinigungen enthaltendem partialoxidationsgas, das zur verwendung in einem kombinierten gas-dampfturbinenkraftwerk bestimmt ist
ATE34201T1 (de) * 1985-08-05 1988-05-15 Siemens Ag Kombiniertes gas- und dampfturbinenkraftwerk.
GB8706077D0 (en) * 1987-03-13 1987-04-15 Boc Group Plc Power generation
AT389526B (de) * 1988-03-15 1989-12-27 Voest Alpine Ind Anlagen Verfahren zur gewinnung von fluessig-roheisen in einem einschmelzvergaser

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JPH0363491A (ja) 1991-03-19
DE69006921T2 (de) 1994-06-09
CA2018238A1 (en) 1990-12-06
EP0402045A1 (en) 1990-12-12
GB8913001D0 (en) 1989-07-26
ES2049925T3 (es) 1994-05-01
DE69006921D1 (de) 1994-04-07
EP0402045B1 (en) 1994-03-02
DK0402045T3 (da) 1994-03-28
JP3188446B2 (ja) 2001-07-16
ATE102335T1 (de) 1994-03-15
US5040370A (en) 1991-08-20
KR0163351B1 (ko) 1998-11-16

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