ZA200702064B - Combined cryogenic distillation and PSA for argon production - Google Patents
Combined cryogenic distillation and PSA for argon production Download PDFInfo
- Publication number
- ZA200702064B ZA200702064B ZA200702064A ZA200702064A ZA200702064B ZA 200702064 B ZA200702064 B ZA 200702064B ZA 200702064 A ZA200702064 A ZA 200702064A ZA 200702064 A ZA200702064 A ZA 200702064A ZA 200702064 B ZA200702064 B ZA 200702064B
- Authority
- ZA
- South Africa
- Prior art keywords
- swing adsorption
- pressure swing
- argon
- adsorption vessel
- gas
- Prior art date
Links
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 title claims description 276
- 229910052786 argon Inorganic materials 0.000 title claims description 138
- 238000004821 distillation Methods 0.000 title claims description 39
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- 239000007789 gas Substances 0.000 claims description 111
- 238000001179 sorption measurement Methods 0.000 claims description 109
- 239000012530 fluid Substances 0.000 claims description 58
- 238000000034 method Methods 0.000 claims description 50
- 230000001105 regulatory effect Effects 0.000 claims description 31
- 238000004891 communication Methods 0.000 claims description 28
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 26
- 239000001301 oxygen Substances 0.000 claims description 26
- 229910052760 oxygen Inorganic materials 0.000 claims description 26
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 239000002808 molecular sieve Substances 0.000 claims description 7
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 59
- 229910052757 nitrogen Inorganic materials 0.000 description 31
- 239000003463 adsorbent Substances 0.000 description 10
- 239000012071 phase Substances 0.000 description 8
- 238000000926 separation method Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- 238000005094 computer simulation Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000004364 calculation method Methods 0.000 description 3
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000004088 simulation Methods 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000001627 detrimental effect Effects 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000004590 computer program Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000001944 continuous distillation Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000007784 solid electrolyte Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
- B01D53/02—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 adsorption, e.g. preparative gas chromatography
- B01D53/04—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 adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/047—Pressure swing adsorption
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B23/00—Noble gases; Compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B23/00—Noble gases; Compounds thereof
- C01B23/001—Purification or separation processes of noble gases
- C01B23/0036—Physical processing only
- C01B23/0052—Physical processing only by adsorption in solids
- C01B23/0057—Physical processing only by adsorption in solids characterised by the adsorbent
- C01B23/0063—Carbon based materials
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes 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
- F25J3/04—Processes 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
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04721—Producing pure argon, e.g. recovered from a crude argon column
- F25J3/04733—Producing pure argon, e.g. recovered from a crude argon column using a hybrid system, e.g. using adsorption, permeation or catalytic reaction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes 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
- F25J3/04—Processes 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
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04721—Producing pure argon, e.g. recovered from a crude argon column
- F25J3/04733—Producing pure argon, e.g. recovered from a crude argon column using a hybrid system, e.g. using adsorption, permeation or catalytic reaction
- F25J3/04739—Producing pure argon, e.g. recovered from a crude argon column using a hybrid system, e.g. using adsorption, permeation or catalytic reaction in combination with an auxiliary pure argon column
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/18—Noble gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/402—Further details for adsorption processes and devices using two beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/416—Further details for adsorption processes and devices involving cryogenic temperature treatment
-
- 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
- C01B2210/0029—Obtaining noble gases
- C01B2210/0034—Argon
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/82—Processes or apparatus using other separation and/or other processing means using a reactor with combustion or catalytic reaction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/58—Processes or apparatus involving steps for recycling of process streams the recycled stream being argon or crude argon
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S62/00—Refrigeration
- Y10S62/923—Inert gas
- Y10S62/924—Argon
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Separation Of Gases By Adsorption (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/372,954 US7501009B2 (en) | 2006-03-10 | 2006-03-10 | Combined cryogenic distillation and PSA for argon production |
Publications (1)
Publication Number | Publication Date |
---|---|
ZA200702064B true ZA200702064B (en) | 2009-08-26 |
Family
ID=38179781
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ZA200702064A ZA200702064B (en) | 2006-03-10 | 2007-03-09 | Combined cryogenic distillation and PSA for argon production |
Country Status (10)
Country | Link |
---|---|
US (1) | US7501009B2 (ru) |
EP (1) | EP1832330B1 (ru) |
KR (1) | KR100837714B1 (ru) |
CN (1) | CN101261072B (ru) |
BR (1) | BRPI0700641B1 (ru) |
RU (1) | RU2434191C9 (ru) |
SA (1) | SA07280095B1 (ru) |
SG (1) | SG136051A1 (ru) |
TW (1) | TWI340122B (ru) |
ZA (1) | ZA200702064B (ru) |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
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US20060236719A1 (en) * | 2005-04-22 | 2006-10-26 | Lane Jonathan A | Gas stream purification method utilizing electrically driven oxygen ion transport |
US7862645B2 (en) * | 2008-02-01 | 2011-01-04 | Air Products And Chemicals, Inc. | Removal of gaseous contaminants from argon |
DE102009003350C5 (de) * | 2009-01-14 | 2017-02-09 | Reicat Gmbh | Verfahren und Vorrichtung zur Abtrennung von Argon aus einem Gasgemisch |
JP2012106904A (ja) * | 2010-10-29 | 2012-06-07 | Sumitomo Seika Chem Co Ltd | アルゴンガスの精製方法および精製装置 |
CN102506560B (zh) * | 2011-09-30 | 2013-07-10 | 浙江新锐空分设备有限公司 | 从废氩气中制取纯氩的方法 |
CN102589252A (zh) * | 2012-03-05 | 2012-07-18 | 苏州市兴鲁空分设备科技发展有限公司 | 氩精馏工艺 |
US9457337B2 (en) | 2013-03-01 | 2016-10-04 | Praxair Technology, Inc. | Adsorbent composition for argon purification |
US9222727B2 (en) | 2013-03-01 | 2015-12-29 | Praxair Technology, Inc. | Purification of argon through liquid phase cryogenic adsorption |
US9644890B2 (en) | 2013-03-01 | 2017-05-09 | Praxair Technology, Inc. | Argon production method and apparatus |
JP6235794B2 (ja) * | 2013-05-28 | 2017-11-22 | 住友精化株式会社 | アルゴン精製方法およびアルゴン精製装置 |
US9676629B2 (en) | 2015-06-09 | 2017-06-13 | Praxair Technology, Inc. | Helium enhanced heat transfer in adsorptive liquid or gas phase argon purification processes |
US10024596B2 (en) | 2015-07-31 | 2018-07-17 | Praxair Technology, Inc. | Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system |
US10012438B2 (en) * | 2015-07-31 | 2018-07-03 | Praxair Technology, Inc. | Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system |
US10066871B2 (en) * | 2015-07-31 | 2018-09-04 | Praxair Technology, Inc. | Method and apparatus for argon rejection and recovery |
US10012437B2 (en) * | 2015-07-31 | 2018-07-03 | Praxair Technology, Inc. | Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system |
US9669349B1 (en) | 2016-02-22 | 2017-06-06 | Air Products And Chemicals, Inc. | Modified chabazite adsorbent compositions, methods of making and using them |
US9925514B2 (en) | 2016-02-22 | 2018-03-27 | Air Products And Chemicals, Inc. | Modified chabazite adsorbent compositions, methods of making and using them |
US20170239641A1 (en) | 2016-02-22 | 2017-08-24 | Air Products And Chemicals, Inc. | Modified Chabazite Adsorbent Compositions, Methods of Making and Using Them |
US9708188B1 (en) | 2016-02-22 | 2017-07-18 | Air Products And Chemicals, Inc. | Method for argon production via cold pressure swing adsorption |
EP3423170B1 (en) * | 2016-03-01 | 2021-05-26 | Praxair Technology, Inc. | Method and apparatus for argon recovery in a cryogenic air separation unit integrated with a pressure swing adsorption system |
US10646848B2 (en) | 2017-09-28 | 2020-05-12 | Air Products And Chemicals, Inc. | RHO adsorbent compositions, methods of making and using them |
US10343139B2 (en) * | 2017-09-28 | 2019-07-09 | Air Products And Chemicals, Inc. | Processes using improved RHO adsorbent compositions |
US10478770B2 (en) * | 2017-12-21 | 2019-11-19 | Air Products And Chemicals, Inc. | Separation process and apparatus for light noble gas |
US11262125B2 (en) | 2018-01-02 | 2022-03-01 | Praxair Technology, Inc. | System and method for flexible recovery of argon from a cryogenic air separation unit |
AU2019202519B2 (en) * | 2019-01-18 | 2020-11-05 | Air Products And Chemicals, Inc. | Separation process and apparatus for light noble gas |
WO2023198307A1 (en) * | 2022-04-14 | 2023-10-19 | Linde Gmbh | Process and apparatus for producing argon from crude argon |
Family Cites Families (27)
Publication number | Priority date | Publication date | Assignee | Title |
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GB1572968A (en) | 1978-05-31 | 1980-08-06 | Air Prod & Chem | Method of purifying crude argon |
US4477265A (en) | 1982-08-05 | 1984-10-16 | Air Products And Chemicals, Inc. | Argon purification |
JPS5992907A (ja) * | 1982-11-19 | 1984-05-29 | Seitetsu Kagaku Co Ltd | 高濃度アルゴンの製造方法 |
US4752311A (en) | 1986-02-24 | 1988-06-21 | The Boc Group, Inc. | Argon recovery from ammonia plant purge gas utilizing a combination of cryogenic and non-cryogenic separating means |
US4687498A (en) | 1986-02-24 | 1987-08-18 | The Boc Group, Inc. | Argon recovery from hydrogen depleted ammonia plant purge gas utilizing a combination of cryogenic and non-cryogenic separating means |
US4750925A (en) | 1986-02-24 | 1988-06-14 | The Boc Group, Inc. | Argon recovery from hydrogen depleted ammonia plant purge gas utilizing a combination of cryogenic and non-cryogenic separating means |
US4732580A (en) | 1986-10-01 | 1988-03-22 | The Boc Group, Inc. | Argon and nitrogen coproduction process |
US4983194A (en) | 1990-02-02 | 1991-01-08 | Air Products And Chemicals, Inc. | Production of high purity argon |
US5100447A (en) | 1990-08-30 | 1992-03-31 | The Boc Group, Inc. | Argon recovery from partial oxidation based ammonia plant purge gases |
US5220797A (en) * | 1990-09-28 | 1993-06-22 | The Boc Group, Inc. | Argon recovery from argon-oxygen-decarburization process waste gases |
US5125934A (en) | 1990-09-28 | 1992-06-30 | The Boc Group, Inc. | Argon recovery from argon-oxygen-decarburization process waste gases |
US5159816A (en) | 1991-05-14 | 1992-11-03 | Air Products And Chemicals, Inc. | Method of purifying argon through cryogenic adsorption |
FR2682611B1 (fr) | 1991-10-17 | 1993-12-03 | Air Liquide | Procede et installation d'epuration d'un gaz par adsorption. |
US5313800A (en) | 1993-02-01 | 1994-05-24 | Praxair Technology, Inc. | Process for maximizing the recovery of argon from an air separation system at high argon recovery rates |
US5601634A (en) | 1993-09-30 | 1997-02-11 | The Boc Group, Inc. | Purification of fluids by adsorption |
CA2142317A1 (en) | 1994-02-24 | 1995-08-25 | Anton Moll | Process and apparatus for the recovery of pure argon |
US5440884A (en) | 1994-07-14 | 1995-08-15 | Praxair Technology, Inc. | Cryogenic air separation system with liquid air stripping |
US5557951A (en) | 1995-03-24 | 1996-09-24 | Praxair Technology, Inc. | Process and apparatus for recovery and purification of argon from a cryogenic air separation unit |
US5827358A (en) * | 1996-11-08 | 1998-10-27 | Impact Mst, Incorporation | Rapid cycle pressure swing adsorption oxygen concentration method and apparatus |
US5738709A (en) | 1996-12-20 | 1998-04-14 | Air Products And Chemicals, Inc. | Nitrogen PSA with intermediate pressure transfer |
US5730003A (en) | 1997-03-26 | 1998-03-24 | Praxair Technology, Inc. | Cryogenic hybrid system for producing high purity argon |
JPH1183309A (ja) | 1997-09-04 | 1999-03-26 | Nippon Air Rikiide Kk | アルゴン精製方法及び装置 |
US6240744B1 (en) | 1999-12-13 | 2001-06-05 | Air Products And Chemicals, Inc. | Process for distillation of multicomponent fluid and production of an argon-enriched stream from a cryogenic air separation process |
US6527831B2 (en) | 2000-12-29 | 2003-03-04 | Praxair Technology, Inc. | Argon purification process |
US6500235B2 (en) | 2000-12-29 | 2002-12-31 | Praxair Technology, Inc. | Pressure swing adsorption process for high recovery of high purity gas |
US6351971B1 (en) | 2000-12-29 | 2002-03-05 | Praxair Technology, Inc. | System and method for producing high purity argon |
US20020139246A1 (en) * | 2001-01-03 | 2002-10-03 | Ravi Kumar | Multi-bed adsorption process for air purification |
-
2006
- 2006-03-10 US US11/372,954 patent/US7501009B2/en active Active
-
2007
- 2007-03-05 SG SG200701712-2A patent/SG136051A1/en unknown
- 2007-03-05 TW TW096107568A patent/TWI340122B/zh active
- 2007-03-07 RU RU2007108561/06A patent/RU2434191C9/ru active
- 2007-03-07 BR BRPI0700641A patent/BRPI0700641B1/pt active IP Right Grant
- 2007-03-09 EP EP07103835.0A patent/EP1832330B1/en active Active
- 2007-03-09 CN CN2007100923952A patent/CN101261072B/zh active Active
- 2007-03-09 ZA ZA200702064A patent/ZA200702064B/en unknown
- 2007-03-09 KR KR1020070023430A patent/KR100837714B1/ko active IP Right Grant
- 2007-03-10 SA SA07280095A patent/SA07280095B1/ar unknown
Also Published As
Publication number | Publication date |
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KR100837714B1 (ko) | 2008-06-13 |
RU2434191C9 (ru) | 2012-05-10 |
RU2007108561A (ru) | 2008-09-20 |
BRPI0700641B1 (pt) | 2017-04-11 |
TWI340122B (en) | 2011-04-11 |
SA07280095B1 (ar) | 2011-01-15 |
EP1832330A2 (en) | 2007-09-12 |
EP1832330A3 (en) | 2010-04-14 |
US20070209508A1 (en) | 2007-09-13 |
CN101261072B (zh) | 2011-07-27 |
BRPI0700641A (pt) | 2007-11-06 |
TW200734270A (en) | 2007-09-16 |
RU2434191C2 (ru) | 2011-11-20 |
EP1832330B1 (en) | 2018-01-17 |
CN101261072A (zh) | 2008-09-10 |
KR20070092664A (ko) | 2007-09-13 |
SG136051A1 (en) | 2007-10-29 |
US7501009B2 (en) | 2009-03-10 |
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