(12) Translation of european patent specification

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1 (12) Translation of european patent specification (11) NO/EP 2403 B1 (19) NO NORWAY (1) Int Cl. C12P 7/06 (06.01) C12N 1/ (06.01) Norwegian Industrial Property Office (21) Translation Published (80) Date of The European Patent Office Publication of the Granted Patent (86) European Application Nr (86) European Filing Date (87) The European Application s Publication Date (30) Priority , US, P (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 SM TR (73) Proprietor Lanzatech New Zealand Limited, 24 Balfour Road Parnell, Auckland 2, NZ-New Zealand (72) Inventor OAKLEY, Simon, David, c/o LanzaTech New Zealand Limited24 Balfour Road, ParnellAuckland 2, NZ-New Zealand (74) Agent or Attorney Jesper Levin A/S, Strandvejen 66, DK-2930 KLAMPENBORG, Danmark (4) Title IMPROVED CARBON CAPTURE IN FERMENTATION (6) References Cited: WO-A1-07/1177 WO-A1-08/80 WO-A2-09/009388

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 (http://worldwide.espacenet.com) or via the search engine on our website here: https://search.patentstyret.no/ NO/EP2403

3 P a t e n t k r a v 1. Framgangsmåte for å øke karbonfangst i en fermenteringsprosess, der framgangsmåten omfatter å forgasse et råmateriale for å produsere et syntesegassubstrat i en forgasser og sette minst en del av syntesegassubstratet i kontakt med én eller flere mikroorganismer i en bioreaktor for å produsere ett eller flere produkter, der produktene er én eller flere syrer og/eller alkoholer, der en utgangsstrøm forlater bioreaktoren og der minst en del av utgangsstrømmen føres inn i forgasseren. 2. Framgangsmåte ifølge krav 1, der utgangsstrømmen omfatter ett eller flere biprodukter av fermentering. 3. Framgangsmåte ifølge krav 2, der et biprodukt av fermentering er karbondioksid, og der minst en del av karbondioksidet som forlater bioreaktoren, ledes til forgasseren. 4. Framgangsmåte ifølge krav 3, der karbondioksid vesentlig separeres fra én eller flere andre komponenter i utgangsstrømmen.. Framgangsmåte ifølge krav 1, der utgangsstrømmen omfatter en første komponent og opsjonelt én eller flere andre komponenter i syntesegasstrømmen som ikke konverteres til produkter ved fermentering Framgangsmåte ifølge krav, der den første komponenten som ikke konverteres til produkter, er metan, og der minst en del av metanet som forlater bioreaktoren, ledes til forgasseren Framgangsmåte ifølge krav 6, der metan vesentlig separeres fra én eller flere komponenter i utgangsstrømmen. 1

4 8. Framgangsmåte for å produsere produkter ved fermentering av et syntesegassubstrat ved hjelp av én eller flere mikroorganismer, der syntesegassen er derivert fra forgassing av et råmateriale og produsert i en forgasser, der framgangsmåten omfatter å lede minst en del av et karbondioksid-biprodukt, produsert i fermenteringen, inn i forgasseren, der produktene er én eller flere syrer og/eller alkoholer. 9. Framgangsmåte i henhold til krav 8, der (a) den ene eller flere syrene omfatter acetat, og/eller (b) den ene eller flere alkoholene omfatter etanol.. Framgangsmåte ifølge et av kravene 1 9, der mikroorganismen(e) er en anaerob karboksydotrof bakterie valgt fra gruppen som består av Clostridium, Moorella, Pyrococcus, Eubacterium, Desulfobacterium, Carboxydothermus, Acetogenium, Acetobacterium, Acetoanaerobium, Butyribaceterium og Peptostreptococcus. 11. Framgangsmåte ifølge krav, der den karboksydotrofe bakterien er Clostridium autoethanogenum som har de identifiserende egenskapene til stammen som er deponert ved Tysk ressurssenter for biologisk materiale (DSMZ) under det identifiserende deponeringsnummeret Framgangsmåte ifølge et av kravene 1 til 7, eller 11, der den ene eller flere syrene og/eller alkoholene er valgt fra gruppen som omfatter acetat og etanol Framgangsmåte ifølge et av kravene 1 12, der råmaterialet omfatter karbonholdig materiale valgt blant: kommunalt fastavfall, skogbruksmateriale, treavfall, byggemateriale, plantemateriale, kull, olje, tremasse og papiravfallmaterialer, petrokjemiske biprodukter, dekk eller kombinasjoner av dette. 2

5 14. System for å øke effektiviteten av en prosess for å produsere produkter som er alkohol(er) og opsjonelt syre(r) ved mikrobiell fermentering av syntesegassubstrater, der systemet omfatter: a. en forgasser som er konfigurert til å produsere et syntesegassubstrat som omfatter CO og H2; b. en bioreaktor som er konfigurert til å konvertere minst en del av CO og opsjonelt H2 fra syntesegassubstratet til produkter; c. midler for å føre minst en del av én eller flere komponenter av syntesegassubstratet som ikke er konvertert til produkt(er), og/eller minst en del av minst ett biprodukt av fermenteringen, fra en utgangsstrøm som forlater bioreaktoren, tilbake til forgasseren.. System ifølge krav 14, der systemet er konfigurert til å føre minst en del av et biprodukt som omfatter karbondioksid, til forgasseren. 16. System ifølge krav 14 eller, der systemet omfatter separasjonsmidler som er konfigurert til å separere karbondioksid fra utgangsstrømmen slik at det kan føres til forgasseren. 3

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