JP5795328B2 - Co2リッチフローを乾燥および圧縮する方法および装置 - Google Patents
Co2リッチフローを乾燥および圧縮する方法および装置 Download PDFInfo
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- 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
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
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- 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
- B01D53/26—Drying gases or vapours
- B01D53/263—Drying gases or vapours by absorption
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- 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
- F25J3/0228—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 characterised by the separated product stream
- F25J3/0266—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 characterised by the separated product stream separation of carbon dioxide
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- 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
- B01D2256/22—Carbon dioxide
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- 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
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
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- 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
- F25J2205/50—Processes or apparatus using other separation and/or other processing means using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil
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- 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/80—Separating impurities from carbon dioxide, e.g. H2O or water-soluble contaminants
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- 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/80—Separating impurities from carbon dioxide, e.g. H2O or water-soluble contaminants
- F25J2220/82—Separating low boiling, i.e. more volatile components, e.g. He, H2, CO, Air gases, CH4
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- 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/80—Separating impurities from carbon dioxide, e.g. H2O or water-soluble contaminants
- F25J2220/84—Separating high boiling, i.e. less volatile components, e.g. NOx, SOx, H2S
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- 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
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/30—Compression of the feed stream
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- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
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- 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/44—Particular materials used, e.g. copper, steel or alloys thereof or surface treatments used, e.g. enhanced surface
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- 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- 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
- Y10S62/928—Recovery of carbon dioxide
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- Thermal Sciences (AREA)
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- Oil, Petroleum & Natural Gas (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- General Engineering & Computer Science (AREA)
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- Carbon And Carbon Compounds (AREA)
- Drying Of Gases (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Treating Waste Gases (AREA)
Description
・3=任意の工程である硫黄含有要素の(およそ1ppmという典型的なレベルへの)精密精製
・5=コンプレッサでの圧縮、湿潤ガスに接触するその材料は耐食鋼からなる
・7=吸着によるガスの乾燥(たとえば活性アルミナ、モレキュラーシーブまたはシリカゲルの吸着剤)
・9=任意にCO2リッチガスから軽い成分(酸素、アルゴン、水素、炭素、一酸化物、窒素、など)および/または重い成分(NO2、N2O4、SO2、など)を取り除く、この工程の考えられる変形は以前の特許出願に詳細に記載している
・11=CO2リッチ最終生成物の圧縮またはCO2リッチ最終生成物の液化により(パイプラインや船舶による)輸送システムに利用したりプロセスに使用したりできるようにする工程
US−A−2862819によって、コンプレッサで圧縮する前に不凍液と混合してから、CO2リッチガスの流れを蒸留により分離することが知られている。
以下に、出願当初の特許請求の範囲の記載事項をそのまま付記しておく。
[1]
水含有CO2リッチ流体を圧縮するにあたり前記CO2リッチ流体をコンプレッサ(5)で圧縮する方法であって、圧縮工程の上流で前記水含有CO2リッチ流体を2つに分け、前記水含有CO2リッチ流体の第1の部分に不凍液を注入し、前記CO2リッチ流体の第2の部分を脱気カラム(2−4)の底部に送って前記カラムからのオーバーヘッドガスを前記不凍液含有CO2リッチ流体の第1の部分と混合し、前記第1の部分を冷却した後に相分離器(2−3)に送り、前記不凍液を含有する水(2−04)を前記相分離器から抽出して前記カラムの頂部に送り、前記相分離器で水を取り除いた冷却流体(2−00)を前記コンプレッサで圧縮する方法。
[2]
前記コンプレッサ(5)は炭素鋼または低合金鋼からなる、請求項1に記載の方法。
[3]
前記不凍液を含有する水を前記カラム(2−4)で処理して不凍液(2−01)の大部分を前記水から抽出し、これを前記冷却工程の上流にリサイクルする、請求項1または2に記載の方法。
[4]
前記コンプレッサ(5)の下流で、圧縮流体を、上流での吸着により乾燥することなく、水の凝固点0℃より低い温度、好ましくは−10℃よりも低い温度で分離する、請求項1ないし3のいずれか1項に記載の方法。
[5]
水リッチの不凍液含有凝縮液(2−05)を0℃より低い温度での分離のあいだに回収し、前記不凍液を抽出後に冷却工程の上流にリサイクルする、請求項4に記載の方法。
[6]
水リッチの不凍液含有凝縮液(2−05)を−10℃より低い温度での前記分離のあいだに回収し、前記不凍液を抽出後に冷却工程の上流にリサイクルする、請求項4に記載の方法。
[7]
前記不凍液を前記カラム(2−4)で抽出する、請求項5および6のいずれかに記載の方法。
[8]
前記CO2リッチ流体(1−00)は、100体積ppm未満の硫黄酸化物または2,000体積ppm未満の硫黄酸化物またはさらに20,000体積ppm未満の硫黄酸化物を含有する、請求項1ないし7のいずれか1項に記載の方法。
[9]
前記相分離器(2−3)の入口でのガスは、−35℃ないし−15℃にあるか、さらに−25℃ないし−15℃にある、請求項1ないし8のいずれか1項に記載の方法。
[10]
水含有CO2リッチ流体を圧縮するユニットであって、コンプレッサ(5)と、前記コンプレッサの上流に、水含有CO2リッチ流体の第1の部分に不凍液を注入する不凍液注入ライン(2−03)と、不凍液含有CO2リッチ流体を冷却する手段(2−2)と、冷却流体から水を抽出する相分離器(2−3)と、脱気カラム(2−4)と、水含有CO2リッチ流体の第2の部分を前記カラムの底部に送る手段と、前記相分離器から前記カラムの頂部に水(2−04)を送る手段と、前記カラムからオーバーヘッドガスを送って前記冷却手段の上流で前記第1の部分と混合させる手段と、水を取り除いた冷却流体を前記コンプレッサに送る手段とを含むことを特徴とするユニット。
[11]
前記コンプレッサは炭素鋼または低合金鋼からなる、請求項10に記載のユニット。
[12]
前記カラムの上流に、前記第2の部分を圧縮するコンプレッサ(2−5)を含む、請求項10および11のいずれかに記載のユニット。
Claims (8)
- 水含有CO2リッチ流体を圧縮するにあたり前記CO2リッチ流体をコンプレッサ(5)で圧縮する方法であって、圧縮工程の上流で前記水含有CO2リッチ流体を2つに分け、前記水含有CO2リッチ流体の第1の部分に不凍液を注入し、前記CO2リッチ流体の第2の部分を脱気カラム(2−4)の底部に送って前記脱気カラム(2−4)からのオーバーヘッドガスを前記不凍液含有CO2リッチ流体の第1の部分と混合し、前記第1の部分を冷却した後に相分離器(2−3)に送り、前記不凍液を含有する水(2−04)を前記相分離器(2−3)から抽出して前記脱気カラム(2−4)の頂部に送り、前記相分離器(2−3)で水を取り除いた冷却流体(2−00)を前記コンプレッサ(5)で圧縮する方法。
- 前記コンプレッサ(5)は炭素鋼または低合金鋼からなる、請求項1に記載の方法。
- 前記不凍液を含有する水(2−04)を前記脱気カラム(2−4)で処理して不凍液(2−01)の大部分を前記不凍液を含有する水(2−04)から抽出し、これを冷却工程の上流にリサイクルする、請求項1または2に記載の方法。
- 前記水含有CO2リッチ流体(1−00)は、100体積ppm未満の硫黄酸化物または2,000体積ppm未満の硫黄酸化物またはさらに20,000体積ppm未満の硫黄酸化物を含有する、請求項1ないし3に記載の方法。
- 前記相分離器(2−3)の入口でのガスは、−35℃ないし−15℃の間にある、請求項1ないし4のいずれか1項に記載の方法。
- 水含有CO2リッチ流体を圧縮するユニットであって、コンプレッサ(5)と、前記コンプレッサ(5)の上流に、水含有CO2リッチ流体を2つに分ける手段と、該2つに分けた前記水含有CO2リッチ流体の第1の部分に不凍液を注入する不凍液注入ライン(2−03)と、不凍液含有CO2リッチ流体を冷却する冷却手段(2−2)と、該冷却された前記不凍液含有CO2リッチ流体から水を抽出する相分離器(2−3)と、脱気カラム(2−4)と、前記2つに分けた水含有CO2リッチ流体の第2の部分を前記脱気カラム(2−4)の底部に送る手段と、前記相分離器(2−3)から前記脱気カラム(2−4)の頂部に不凍液を含有する水(2−04)を送る手段と、前記脱気カラム(2−4)からオーバーヘッドガスを送って前記冷却手段(2−2)の上流で前記第1の部分と混合させる手段と、前記相分離器(2−3)で水を取り除いた冷却流体(2−00)を前記コンプレッサ(5)に送る手段とを含むことを特徴とするユニット。
- 前記コンプレッサ(5)は炭素鋼または低合金鋼からなる、請求項6に記載のユニット。
- 前記脱気カラム(2−4)の上流に、前記第2の部分を圧縮するコンプレッサ(2−5)を含む、請求項6または7に記載のユニット。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0959370A FR2954179B1 (fr) | 2009-12-22 | 2009-12-22 | Procede et appareil de sechage et de compression d'un flux riche en co2 |
FR0959370 | 2009-12-22 | ||
PCT/FR2010/052858 WO2011086289A1 (fr) | 2009-12-22 | 2010-12-21 | Procédé et appareil de séchage et de compression d'un flux riche en co2 |
Publications (2)
Publication Number | Publication Date |
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JP2013515232A JP2013515232A (ja) | 2013-05-02 |
JP5795328B2 true JP5795328B2 (ja) | 2015-10-14 |
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JP2012545391A Expired - Fee Related JP5795328B2 (ja) | 2009-12-22 | 2010-12-21 | Co2リッチフローを乾燥および圧縮する方法および装置 |
Country Status (10)
Country | Link |
---|---|
US (1) | US8852318B2 (ja) |
EP (1) | EP2516041B1 (ja) |
JP (1) | JP5795328B2 (ja) |
CN (1) | CN102665864B (ja) |
AU (1) | AU2010342341B2 (ja) |
CA (1) | CA2784742A1 (ja) |
ES (1) | ES2486293T3 (ja) |
FR (1) | FR2954179B1 (ja) |
WO (1) | WO2011086289A1 (ja) |
ZA (1) | ZA201203624B (ja) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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FR2961270B1 (fr) * | 2010-06-11 | 2017-07-28 | Air Liquide | Procede et appareil de sechage et de compression d'un flux riche en co2 |
FR2978439B1 (fr) * | 2011-07-25 | 2015-11-06 | Air Liquide | Procede et appareil de refroidissement et de compression d'un gaz humide riche en dioxyde de carbone |
DE102011084733A1 (de) * | 2011-10-18 | 2013-04-18 | Victoria Capital Investments Group LTD. | Verfahren und Vorrichtung zur Entwässerung eines C02-haltigen Gases |
FR3118717A1 (fr) | 2021-01-14 | 2022-07-15 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Procédé et appareil de séchage d’un débit riche en dioxyde de carbone |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2862819A (en) * | 1954-08-05 | 1958-12-02 | Miller Brewing | Apparatus for and method of removing impurities from highly volatile gas |
NL251816A (ja) * | 1959-05-21 | 1900-01-01 | ||
JPS5532784A (en) * | 1978-08-31 | 1980-03-07 | Seitetsu Kagaku Co Ltd | Production of liquefied carbon dioxide |
US4252548A (en) * | 1979-01-02 | 1981-02-24 | Kryos Energy Inc. | Carbon dioxide removal from methane-containing gases |
DE3416519A1 (de) * | 1983-05-20 | 1984-11-22 | Linde Ag, 6200 Wiesbaden | Verfahren und vorrichtung zur zerlegung eines gasgemisches |
US4704146A (en) * | 1986-07-31 | 1987-11-03 | Kryos Energy Inc. | Liquid carbon dioxide recovery from gas mixtures with methane |
JPH07108368B2 (ja) * | 1990-11-02 | 1995-11-22 | 住友精化株式会社 | 混合ガス中の水分除去方法 |
US20020117391A1 (en) * | 2001-01-31 | 2002-08-29 | Beam Craig A. | High purity CO2 and BTEX recovery |
GB2416389B (en) * | 2004-07-16 | 2007-01-10 | Statoil Asa | LCD liquefaction process |
WO2006037320A1 (en) * | 2004-10-08 | 2006-04-13 | Union Engineering A/S | Method for recovery of carbon dioxide from a gas |
FR2912207B1 (fr) * | 2007-02-01 | 2012-10-26 | Air Liquide | Procede et appareil de production de monoxyde de carbone par distillation cryogenique |
US7819932B2 (en) * | 2008-04-10 | 2010-10-26 | Carbon Blue-Energy, LLC | Method and system for generating hydrogen-enriched fuel gas for emissions reduction and carbon dioxide for sequestration |
EP2328673A1 (en) * | 2008-07-16 | 2011-06-08 | Union Engineering A/S | Method for purification of carbon dioxide using liquid carbon dioxide |
AU2011274797B2 (en) * | 2010-07-09 | 2015-05-21 | Arnold Keller | Carbon dioxide capture and liquefaction |
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2009
- 2009-12-22 FR FR0959370A patent/FR2954179B1/fr not_active Expired - Fee Related
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2010
- 2010-12-21 ES ES10808911.1T patent/ES2486293T3/es active Active
- 2010-12-21 EP EP10808911.1A patent/EP2516041B1/fr not_active Not-in-force
- 2010-12-21 CN CN201080058260.4A patent/CN102665864B/zh not_active Expired - Fee Related
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- 2010-12-21 WO PCT/FR2010/052858 patent/WO2011086289A1/fr active Application Filing
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Also Published As
Publication number | Publication date |
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JP2013515232A (ja) | 2013-05-02 |
WO2011086289A1 (fr) | 2011-07-21 |
AU2010342341B2 (en) | 2014-06-19 |
FR2954179A1 (fr) | 2011-06-24 |
EP2516041B1 (fr) | 2014-04-30 |
ZA201203624B (en) | 2013-01-30 |
EP2516041A1 (fr) | 2012-10-31 |
CN102665864B (zh) | 2014-11-05 |
US8852318B2 (en) | 2014-10-07 |
ES2486293T3 (es) | 2014-08-18 |
CN102665864A (zh) | 2012-09-12 |
CA2784742A1 (fr) | 2011-07-21 |
AU2010342341A1 (en) | 2012-07-05 |
FR2954179B1 (fr) | 2014-03-28 |
US20120272680A1 (en) | 2012-11-01 |
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