(12) Translation of European patent specification

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1 (12) Translation of European patent specification (11) NO/EP B1 (19) NO NORWAY (51) Int Cl. C02F 3/00 ( ) C02F 1/52 ( ) C02F 3/30 ( ) C05B 7/00 ( ) C05F 17/00 ( ) C05F 17/02 ( ) C02F 1/12 ( ) C02F 1/66 ( ) C02F 9/00 ( ) C02F 11/04 ( ) C02F 11/12 ( ) C02F 101/10 ( ) C02F 101/32 ( ) C02F 101/34 ( ) 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, (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 Clean Water Services, Gaffi, Bill 2550 SW Hillsboro Highway, Hillsboro, OR 97123, US-USA (72) Inventor BAUR, Robert, 2550 SW Hillsboro Highway, Hillsboro, OR 97123, US-USA (74) Agent or Attorney Protector Intellectual Property Consultants AS, Oscarsgate 20, 0352 OSLO, Norge (54) Title Waste activated sludge phosphorus and magnesium stripping process and struvite production system (56) References Cited: WO-A2-2007/ DE-A US-A US-A US-A US-A US-B M. R. GATERELL ET AL: "An economic and environmental evaluation of the opportunities for substituting phosphorus recovered from wastewater treatment works in existing UK fertiliser markets", ENVIRONMENTAL TECHNOLOGY, vol. 21, no. 9, 1 January 2000 ( ), pages , XP , S. WILLIAMS: "Struvite Precipitation in the Sludge Stream at Slough Wastewater Treatment Plant and Opportunities for Phosphorus Recovery", ENVIRONMENTAL TECHNOLOGY, vol. 20,

2 no. 7, 1 January 1999 ( ), pages , XP , M. R. Gaterell ET AL: "An Economic and Environmental Evaluation of the Opportunities for Substituting Phosphorus Recovered from Wastewater Treatment Works in Existing UK Fertiliser Markets", Environmental Technology, vol. 21, no. 9, 1 September 2000 ( ), pages , XP , ISSN: , DOI: / 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 hee:

3 1 P a t e n t k r a v Fremgangsmåte for behandling av avfall, innbefattende (a) fremstille en første blanding av faststoff, mikroorganismer og væske fra avløpsvann, og hvor nevnte mikroorganismer inneholder fosfor og magnesium; (b) fjerne fosfor og magnesium fra mikroorganismene og tillate at de fjernede fosforet og magnesiumet oppløses i en flytende del av den første blandingen, hvor fjerningstrinnet innbefatter tilsetting av lett biologisk nedbrytbare karbonforbindelser (RBC er) til den første blandingen, og derved fremstille en behandlet blanding som innbefatter oppløst magnesium og fosfor; (c) fermentere og fortykke den behandlede blandingen for å fremstille en fosfor-rik og magnesium-rik væske som er separert fra en gjenværende fosfor-redusert og magnesium-redusert blanding; (d) videre anaerobt behandle den fosfor-reduserte og magnesium-reduserte blandingen og derved danne en ammoniakk-rik væske; (e) avvanne den og ammoniakk-rike blandingen for å danne en ammoniakkrik væske (f) blande den ammoniakk-rike væsken med den fosfor-rike og magnesiumrike væsken, for å danne struvitt Fremgangsmåte i henhold til krav 1, hvor trinn (b) blir utført ved å holde den behandlede væsken i en anaerob reaktor i minst 0,5 timer Fremgangsmåte i henhold til krav 1, hvor RBC ene innbefatter flyktige fettsyrer (VFA er). 4. Fremgangsmåte i henhold til krav 1, hvor RBC ene innbefatter forbindelser som blir omdannet til flyktige fettsyrer (VFA er) av mikroorganismene.

4 2 5. Fremgangsmåte i henhold til krav 1, hvor den første blandingen er avfallsaktivert slam Fremgangsmåte i henhold til krav 1, hvor den første blandingen er blandede væskesuspenderte faststoffer Fremgangsmåte i henhold til krav 1, hvor trinn (b) blir utført ved å føre den første blandingen gjennom en anaerob sone, hvor det er tilstede flyktige fettsyrene som medfører at fosfor og magnesium blir utstøtt fra mikroorganismene Fremgangsmåte i henhold til krav 1, hvor trinn (b) blir utført ved å holde tilbake den første blandingen i en anaerob reaktor i mer enn 36 timer Fremgangsmåte i henhold til krav 1, hvor trinnet med blanding av den magnesium- og fosfor-rike væsken med den ammoniakk-rike væsken blir utført i en struvitt-reaktor og hvor magnesiumet blir tilsatt til struvitt-reaktoren eller enhver tilførsel derav, for derved å øke dannelsen av struvitt Fremgangsmåte i henhold til krav 1, hvor den ammoniakk-rike væsken blir blandet med den fosfor-rike og magnesium-rike væsken på en måte som danner et anvendelig struvitt-produkt Fremgangsmåte i henhold til krav 1, hvor den fosfor-reduserte og magnesiumreduserte blandingen fremstilt i trinn (c) er i form av et slam, og hvor trinn (d) blir utført med slammet fremstilt i trinn (c) blandet med minst et annet slam fra avfallsbehandlingsprosessen.

5 3 12. Fremgangsmåte i henhold til krav 1, hvor trinnene (a), (b), (c), (d), (e) og (f) blir utført in situ.

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