| CPC C02F 9/00 (2013.01) [C01B 25/26 (2013.01); C01B 25/265 (2013.01); C05F 3/00 (2013.01); C05F 17/15 (2020.01); C05F 17/40 (2020.01); C05F 17/50 (2020.01); C02F 1/20 (2013.01); C02F 1/74 (2013.01); C02F 3/28 (2013.01); C02F 3/341 (2013.01); C02F 11/04 (2013.01); C02F 11/125 (2013.01); C02F 11/126 (2013.01); C02F 11/145 (2019.01); C02F 11/18 (2013.01); C02F 2101/101 (2013.01); C02F 2101/105 (2013.01); C02F 2101/16 (2013.01); C02F 2103/20 (2013.01); C02F 2209/02 (2013.01); C02F 2209/06 (2013.01); C05F 17/10 (2020.01); Y02A 40/20 (2018.01); Y02E 50/30 (2013.01); Y02P 20/145 (2015.11); Y02W 30/40 (2015.05)] | 20 Claims |

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1. A method for phosphate recovery from a waste stream, comprising the steps of:
providing a tank reactor;
providing acidogenic bacteria and/or acetogenic bacteria and providing the waste stream to the tank reactor;
hydrolysing the waste stream, and forming a reaction mixture with a compound comprising phosphate;
providing a gas flow to the reaction mixture for removing carbon dioxide from the reaction mixture;
providing the reaction mixture to an anaerobic sludge reactor;
removing the compound comprising phosphate from the reaction mixture within the anaerobic sludge reactor; and
removing gas from the reaction mixture within the anaerobic sludge reactor.
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