(12) Translation of european patent specification

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1 (12) Translation of european patent specification (11) NO/EP B1 (19) NO NORWAY (1) Int Cl. F23J /02 (06.01) B01D 3/34 (06.01) B01D 3/62 (06.01) Norwegian Industrial Property Office (21) Translation Published (80) Date of The European Patent Office Publication of the Granted Patent.04. (86) European Application Nr (86) European Filing Date (87) The European Application s Publication Date (30) Priority , US, , US, (84) Designated Contracting States: AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK TR (73) Proprietor ALSTOM Technology Ltd, Brown Boveri Strasse 7, 400 Baden, CH-Sveits (72) Inventor JUKKOLA, Glen D., Shagbark Road, Glastonbury, Connecticut 06033, US-USA ANDRUS, JR., Herbert E., 94 Hungary Road, Granby, Connecticut 0603, US-USA MCCARTNEY, Michael S., 4th Court S.W., Vero Beach, Florida 32968, US- USA (74) Agent or Attorney Tandbergs Patentkontor AS, Postboks 70 Vika, 0118 OSLO, Norge (4) Title REDUCING CARBON DIOXIDE (CO2) EMISSIONS FROM THE BURNING OF A FOSSIL FUEL (6) References Cited: US-A US-B

2 Enclosed is a translation of the patent claims in Norwegian. Please note that as per the Norwegian Patents Acts, section 66i the patent will receive protection in Norway only as far as there is agreement between the translation and the language of the application/patent granted at the EPO. In matters concerning the validity of the patent, language of the application/patent granted at the EPO will be used as the basis for the decision. The patent documents published by the EPO are available through Espacenet ( or via the search engine on our website here:

3 1 Patentkrav EP Et system () for å redusere utslipp av karbondioksid fra gasser som dannes ved forbrenning av fossilt brensel, hvor systemet () omfatter: 30 3 en beholder () som er konfigurert for å lede gasser som genereres ved forbrenning av fossilt brensel i en oppadgående strømning og med et øvre første parti (12,14) og et nedre andre parti (0), der det øvre første parti (12,14) omfatter en nedre forbrenningssone (14) for forbrenning av fossilt brensel (16) og en øvre reaksjonssone (12) for å fange karbondioksid (CO 2 ), der det nedre andre parti inkludert en gjenoppvarmer (0), hvorved den øvre reaksjonssonen (12) mottar en første type faste partikler og andre type faste partikler, der den første typen av faste partikler er i stand til å absorbere varme fra gassene og å strømme nedover fra det øvre partiet til det nedre partiet gjennom beholderen til et andre beholderutløp og den andre typen faste partikler er i stand til å fange opp karbondioksid fra gassene og å reagere med oppad strømmende gasser (22) for å absorbere CO 2 fra den oppad strømmende gass (22), der hastigheten til de oppad strømmende gasser er tilstrekkelig til å forårsake at den andre typen av faste partikler strømmer med gassene til et første beholderutløp (36), en separator (38) som skiller den andre typen faste partikler med fanget CO 2 fra de oppad strømmende gasser (22) som slippes ut fra det første beholderutløpet (36), og leder den separerte andre typen faste partikler med det fangede CO 2 -utslipp til et separatorutløp (3), for tømming av den andre typen faste partikler med det fangede karbondioksid fra separatorens utløp i en nedad gående strøm til en første gjenoppvarmers utløp; og et avløp som tillater strømning av den første typen faste partikler med absorbert varme fra forbrenningssonen (14) til gjenoppvarmeren (0) og forhindrer strømmen av den andre type av faste partikler og gjenværende faste partikler til den oppad strømmende gass (22) fra forbrenningssonen (14) til gjenoppvarmeren (0); der varmen leveres av den første typen faste partikler som gir energi til å varme de andre typer faste partikler med den fangede CO 2 gitt fra separatorens utløp (3) for å separere CO 2 fra denne, og CO 2 som er rettet mot en gjenoppvarmer sitt utløp ().

4 2 2. System () ifølge krav 1, der: den første typen faste partikler inkluderer bauxitt; og den andre typen av de faste partiklene omfatter kalkstein. 3. System () ifølge krav 1, der: den andre typen faste partikler er CaO-partikler; og den andre typen faste partikler med det fangede CO 2 er CaCO 3 partikler. 4. System () ifølge krav 1, der: gjenoppvarmeren (0) er en kalsinator; og separatoren (38) er en syklon.. System () ifølge krav 1, der den nedad gående strøm av mottatte første type faste partikler er en tyngdekraftbasert strøm. 6. System () ifølge krav 1, der avløpet inkluderer: 30 3 et rør (31) som har en øvre åpning (31a) som er konfigurert til å motta den nedad strømmende første typefaste partikler med den absorberte varme fra den nedre forbrenningssone (14), og en nedre åpning (31b) konfigurert til å slippe ut nedad strømmende faste partikler av første type med den absorberte varme inn i gjenoppvarmeren (0); og en apertur (49) for å motta en strøm av luft, som har en hastighet, gjennom aperturen (49) og gjennom røret (31) for å lede den første type faste partikler med den absorberte varme i en nedad gående strøm fra den øvre åpning (31a) til den nedre åpningen (31B), der hastigheten til de mottatte luftstrømmer rettet mot røret (31) er utilstrekkelig for å hindre den nedad gående strøm av den første typen faste partikler med den absorberte varme fra å gå gjennom røret (31) fra den øvre åpningen (31a) til den nedre åpningen (31b) og er tilstrekkelig for å hindre at frigjort CO 2 går gjennom røret (31) fra den nedre åpningen (31b) til den øvre åpningen (31a) og derved entrer forbrenningssonen (14). 7. En fremgangsmåte for å redusere utslipp av karbondioksid fra gasser som dannes ved forbrenning av fossilt brensel, hvor fremgangsmåten omfatter: å forbrenne fossilt brensel (16) i en nedre forbrenningssone (14) til et øvre første parti (12,14) av en beholder ();

5 3 å fange karbondioksid (CO 2 ) i en øvre reaksjonssone (12) til et øvre første parti (12,14) til en beholder (); å motta første type faste partikler og andre type faste partikler i den øvre reaksjonssonen (12); å strømme den første type av faste partikler nedad gjennom beholderen () slik at varme fra de oppover strømmende gasser absorberes av den nedad gående strøm av første type faste partikler, der hastigheten av de oppad strømmende gasser er tilstrekkelig til å hindre den nedad gående strøm av den første type faste partikler; å reagere den andre type av faste partikler med oppad strømmende gasser (22) for å absorbere CO 2 fra den oppad strømmende gass (22); å separere i en separator (38) den andre type faste partikler med fanget CO2 fra de oppad strømmende gasser (22) sluppet ut fra et første beholderutløp (36); å lede de separerte andre typer faste partikler med fanget CO 2 til et separatorutløp (3); å tillate strøm av den første type av faste partikler med absorbert varme fra forbrenningssonen (14) til en gjenoppvarmingsenhet (0) i det nedre andre parti (0) av beholderen () på grunn av at den oppad strømmende gasshastigheten er tilstrekkelig til å hindre nevnte partikler; å hindre strømmen av den andre type av faste partikler og gjenværende faste partikler til den oppad strømmende gass (22) fra forbrenningssonen (14) til gjenoppvarmeren (0) på grunn av at hastigheten til den oppad strømmende gass; å oppvarme den andre type faste partikler med den fangede CO 2 gitt fra separatorens utløp (3) med varme levert av den første typen av faste partikler for å separere CO 2 fra denne; og å lede CO 2 i en oppad gående strøm til en gjenoppvarmers utløp (). 8. Fremgangsmåte ifølge krav 7, der: 30 den første type faste partikler inkluderer bauxitt; og den andre type faste partikler omfatter kalkstein. 9. Fremgangsmåte ifølge krav 7, der: 3 den andre typen faste partikler er CaO-partikler; og den andre type faste partikler med den fangede CO 2 er CaCO 3 -partikler.

6 4. Fremgangsmåte ifølge krav 7, der: gjenoppvarmeren (0) er en kalsinator; og separatoren (38) er en syklon. 11. Fremgangsmåte ifølge krav 7, der den frigitte CO2 i gjenoppvarmeren (0) er hovedsakelig ren karbondioksid. 12. Fremgangsmåte ifølge krav 7, der den nedad gående strøm til de mottatte første typer faste partikler er en tyngdekraftbasert strøm. 13. Fremgangsmåte ifølge krav 7, der: de oppad strømmende gasser (22) i beholderen () varmer opp det øvre parti (12) av beholderen til en temperatur innenfor et område på 8K (00 grader Fahrenheit) til 33K (1400 grader Fahrenheit); og den andre type faste partikler fanger CO 2 fra gassene ved temperaturen. 14. Fremgangsmåte ifølge krav 7, der: strømmen av den første type faste partikler med den absorberte varme varmer gjenoppvarmeren (0) til en temperatur innenfor et område på 1K (1800 grader Fahrenheit) til 1366K (00 grader Fahrenheit); og det fangede CO 2 frigjøres fra andre type faste partikler ved temperaturen.

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