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HRP20120848T1 - Postupak i uređaj za ponovnu preradu ispušnih plinova koji sadrže co - Google Patents

Postupak i uređaj za ponovnu preradu ispušnih plinova koji sadrže co Download PDF

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Publication number
HRP20120848T1
HRP20120848T1 HRP20120848AT HRP20120848T HRP20120848T1 HR P20120848 T1 HRP20120848 T1 HR P20120848T1 HR P20120848A T HRP20120848A T HR P20120848AT HR P20120848 T HRP20120848 T HR P20120848T HR P20120848 T1 HRP20120848 T1 HR P20120848T1
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Croatia
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gas
shaft
bulk material
pyrolytic
pressure
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HRP20120848AT
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Roland Möller
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Ecoloop Gmbh
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Publication of HRP20120848T1 publication Critical patent/HRP20120848T1/hr

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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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/62—Carbon oxides
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/06—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated according to the moving bed type
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C10J3/06—Continuous processes
    • C10J3/14—Continuous processes using gaseous heat-carriers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
    • C10J3/60—Processes
    • C10J3/64—Processes with decomposition of the distillation products
    • C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0916—Biomass
    • C10J2300/092—Wood, cellulose
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/093—Coal
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0959—Oxygen
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0969—Carbon dioxide
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0983—Additives
    • C10J2300/0996—Calcium-containing inorganic materials, e.g. lime
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1807—Recycle loops, e.g. gas, solids, heating medium, 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
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
    • 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
    • Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biomedical Technology (AREA)
  • Materials Engineering (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treating Waste Gases (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Chemical Vapour Deposition (AREA)
  • Industrial Gases (AREA)

Claims (14)

1. Postupak ponovne prerade otpadnih plinova koji sadrže CO2 u postupku redukcije u više koraka, gdje se otpadni plin koji sadrži CO2 provodi protustrujno kretanju krute mase od rasutog materijala koji se ne može pretvoriti u plin i toplinski razgradljive organske mase, koja ne sadrži isključivo ugljen, kroz više zona (4, 3, 2, 1) sve do u zonu za izjednačavanje tlaka, te tako prevodi u pirolitičke plinove, naznačen time što se, u smjeru protoka kretanja krute mase, a) u koraku generiranja plinovitog goriva (1) na 250-700 °C organsku masu toplinski razgrađuje u redukcijskim uvjetima u ugljikovodike kratkog lanca, vodik i ugljični monoksid, uz dobivanje koksa i ostatka, b) u međukoraku (2), uz porast temperature, koks oksidira, gdje se dobiveni ugljični monoksid ispušta suprotno kretanju krute mase u korak generiranja plinovitog goriva (1), c) u koraku generiranja ugljičnog monoksida (3) na 800-1600 °C ostatke preostalog koksa u potpunosti pomoću ugljičnog dioksida prevodi u ugljični monoksid, gdje se tlak i temperaturu podešava u skladu s Boudouardovom ravnotežom, d) u koraku hlađenja (4) krute ostatke i grube komade rasutog materijala koji se ne može pretvoriti u plin se ohlade ispod 100 °C u protustruji CO2, te izbacuje iz postupka, e) nakon uklanjanja u najmanju ruku nerasplinjivi rasuti materijal izbačen iz postupka vraća u krug.
2. Postupak u skladu s patentnim zahtjevom 1, naznačen time što se u međukoraku (2) uspostavlja temperatura od 600-1000 °C, a tlak se snižava, tako da se piroliza organske mase i reakcija s Boudouardovom ravnotežom provodi zajedno pod niskim tlakom i na niskoj temperaturu u ovom koraku.
3. Postupak u skladu s patentnim zahtjevom 2, naznačen time što se pirolitički plin izvlači sisaljkom (20), čime se postiže sniženi tlak u međukoraku.
4. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se, u zoni za izjednačavanje tlaka (32) iznad koraka generiranja plinovitog goriva (1), smjesa grubog i fino razdijeljenog rasutog materijala upotrebljava kao spremnik tlaka.
5. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se temperatura i tlak kontroliraju pomoću sastava krutih masa i/ili brzinom njihovog protoka.
6. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se temperatura i tlak kontroliraju omjerom između dodane toplinski razgradljive organske mase i CO2 i izborno dodanog plina koji sadrži kisik.
7. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se izvor ugljika dodatno umiješa u tijek krute mase.
8. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se u koraku hlađenja (4), u međukoraku (2) ili u koraku s ugljičnim monoksidom (3) dodaje voda i/ili vodena para.
9. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se postupak redukcije u više koraka provodi u peći za kalciniranje s oknom (10), gdje se rasuti materijal sipa odozgo, niz okno peći, tako da se pirolitičke plinove i pirolitički koks koji sadrže komponente koje sadrže ugljik toplinski cijepa uz pomno isključivanje kisika kako bi se dobile molekule kratkih lanaca s duljinom lanca <C4, gdje se nastale pirolitičke plinove ispušta iz peći za kalciniranje s oknom, a upotrijebljeni rasuti materijal po mogućnosti sadrži bazične produkte kalciniranja, njihove preteče ili inertne rasute materijale, po mogućnosti u obliku živog vapna (CaO).
10. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se, radi vraćanja u krug, rasuti materijal s rasponom veličina čestica od 0,5-15 cm izbacuje iz postupka nakon uklanjanja iz koraka hlađenja.
11. Postupak u skladu s patentnim zahtjevom 10, naznačen time što se vraćeni fini prah, koji sadrži pirolitičke ostatke vezane na fino razdijeljeni rasuti materijal, uklanja iz pirolitičkih plinova filtriranjem plina (22).
12. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se pirolitičke plinove upotrebljava kao sintezni plin (26) za kemijske procese i/ili za toplinsko recikliranje, pirolitičke plinove razdvaja djelomičnim ukapljivanjem i/ili adsorcijom uz promjenjivi tlak u njihove plinovite komponente ugljični monoksid, ugljični dioksid, vodik i ugljikovodike, gdje se ugljični monoksid upotrebljava kao plin za sintezu (26) za recikliranje materijala u kemijskim procesima, odvojeni vodik se upotrebljava za grijanje i/ili recikliranje materijala i/ili ugljikovodike (28) se upotrebljava za grijanje i/ili recikliranje materijala i/ili kao motorna goriva, ili pirolitičke plinove uglavnom prevodi u vodik i ugljični dioksid reakcijom plina za sintezu (30), katalitčkom reakcijom ispod 500 °C s vodenom parom, gdje se navedeni vodik i ugljični dioksid razdvaja postupcima fizičkog razdvajanja, gdje se vodik upotrebljava za grijanje i/ili recikliranje materijala, a dobiveni CO2 se djelomično recirkulira kako bi se dobila protustruju.
13. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se otpadni plin koji sadrži CO2 kojeg treba ponovno preraditi generira u postupku izgaranja, gdje se upotrebljavaju fosilna goriva, a pirolitički plinovi koji nastaju prilikom ponovne prerade se pak upotrebljavaju u postupku izgaranja, ili se otpadni plin koji sadrži CO2 generira u postupku kalciniranja (5, 6, 7, 8), gdje se karbonate prevodi u okside uklanjanjem CO2, gdje se pirolitički plinovi (20) koji nastaju prilikom ponovne prerade upotrebljavaju kako bi se osiguralo dio toplinske energije potrebne za postupak kalciniranja.
14. Uređaj za provođenje postupka u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što se sastoji od peći s okomitim oknom (10), gdje je ulazno okno (32) za protok materijala postavljeno na gornjem kraju, a uređaj za izbacivanje (14) krutih ostataka i pepela je postavljen na donjem kraju, gdje ulazno okno (32) ima okomiti spust, koji je kao spremnik za izjednačavanje tlaka ispunjen smjesom rasutog materijala koji se ne može pretvoriti u plin i toplinski razgradljive organske mase, gdje je, u gornjem dijelu (1) peći s oknom (10), postavljena sisaljka (20) i separator (22) za plin i fino razdijeljene čestice i, u središnjem dijelu (3), dovodi plinovitog goriva (34) za kontroliranje temperature peći otvoreno u okno (10), te gdje su, na donjem kraju (14) peći s oknom (10), postavljeni dovodi plina (12, 13) za CO2 i plin koji sadrži kisik, opremljeni regulatorima protoka kako bi se uspostavilo Boudouardovu ravnotežu u peći s oknom (10), gdje je postavljen i dodatni uređaj (16), koji, iza uređaja za izbacivanje (14), razdvaja rasuti materijal koji se ne može pretvoriti u plin od krutih ostataka i vraća ga u ulazno okno (32).
HRP20120848AT 2007-12-20 2008-12-18 Postupak i uređaj za ponovnu preradu ispušnih plinova koji sadrže co HRP20120848T1 (hr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102007062413A DE102007062413B3 (de) 2007-12-20 2007-12-20 Verfahren und Vorrichtung zur Wiederaufbereitung von CO2-haltigen Abgasen
PCT/EP2008/010869 WO2009080297A1 (de) 2007-12-20 2008-12-18 Verfahren und vorrichtung zur wiederaufbereitung von co2-haltigen abgasen

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HRP20120848T1 true HRP20120848T1 (hr) 2012-12-31

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US (1) US8911520B2 (hr)
EP (1) EP2227312B1 (hr)
JP (1) JP5581217B2 (hr)
KR (1) KR101342226B1 (hr)
CN (1) CN101903081B (hr)
AU (1) AU2008340650B2 (hr)
BR (1) BRPI0820734A2 (hr)
CA (1) CA2708860C (hr)
CY (1) CY1113815T1 (hr)
DE (1) DE102007062413B3 (hr)
DK (1) DK2227312T3 (hr)
ES (1) ES2393149T3 (hr)
HR (1) HRP20120848T1 (hr)
PL (1) PL2227312T3 (hr)
PT (1) PT2227312E (hr)
RS (1) RS52604B (hr)
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ZA201003942B (en) 2011-03-30
JP5581217B2 (ja) 2014-08-27
RU2010129543A (ru) 2012-01-27
WO2009080297A1 (de) 2009-07-02
CN101903081B (zh) 2014-08-06
EP2227312A1 (de) 2010-09-15
PT2227312E (pt) 2012-10-31
HK1148497A1 (en) 2011-09-09
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DE102007062413B3 (de) 2009-09-10
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