# US 11,440,825 B2 · Struvite recovery and phosphorus management techniques for wastewater treatment plants > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,440,825 B2 - Document ID: US11440825B2 - Status: Granted - Kind: B2 - Application number: 16/157,366 - Filed: 2018-10-11 - Published: 2019-04-11 - Granted: 2022-09-13 - Earliest claimed: 2017-10-11 - Assignees: Schwing Bioset, Inc. - Applicants: Schwing Bioset, Inc. - Inventors: Charles M. Wanstrom; Thomas M. Anderson; Wim H. M. Moerman - Web page: https://patentgrep.com/patent/US11440825B2 ## CPC - C02F 9/00: Multistage treatment of water, waste water or sewage - C02F 1/66: by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) - C02F 3/286: {including two or more steps} - C02F 11/04: Anaerobic treatment; Production of methane by such processes - C02F 11/12: by de-watering, drying or thickening - C02F 2101/105: {Phosphorus compounds} - C02F 2301/106: Thermophilic treatment - C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes) ## Abstract A waste treatment process utilizes a two-stage digestion process with a thermophilic digester, a heat exchanger, and a mesophilic digester. The pH of the thermophilic digestate is increased by removal of carbon dioxide with an air stripper, or by adding a pH increasing reagent upstream of the heat exchanger. The pH adjustment of the digestate protects the heat exchanger and downstream equipment and processes from struvite formation. A struvite reactor may be located in various locations downstream of the heat exchanger to produce a treated digestate or effluent that contains struvite, which can optionally be recovered for beneficial use. ## Claims ### Claim 1 A waste treatment process comprising: supplying waste activated sludge through a heat exchanger to a thermophilic digester; processing the waste activated sludge received from the heat exchanger in a thermophilic digester to produce a thermophilic digestate; increasing pH of the thermophilic digestate downstream of the thermophilic digester; concurrently with increasing pH of the thermophilic digestate and prior to any other processing, cooling the thermophilic digestate in the heat exchanger by heat transfer from the thermophilic digestate to the waste activated sludge; processing the pH increased and cooled thermophilic digestate in a mesophilic digester to produce a mesophilic digestate downstream of the heat exchanger and prior to any other processing; producing, with a struvite reactor, a treated digestate containing struvite; and separating struvite from the treated digestate; wherein increasing pH of the thermophilic digestate downstream of the thermophilic digester inhibits struvite scaling during cooling the thermophilic digestate in the heat exchanger and processing the pH increased and cooled thermophilic digestate in the mesophilic digester. ### Claim 2 (depends on 1) The waste treatment process of claim 1, wherein separating struvite comprises: dewatering treated digestate from the struvite reactor to separate effluent and biosolids enriched with struvite. ### Claim 3 (depends on 2) The waste treatment process of claim 2, wherein separating struvite further comprises: separating with a cyclone separator supplied by a pump between the struvite reactor and the cyclone separator, struvite from the treated digestate prior to dewatering. ### Claim 4 (depends on 1) The waste treatment process of claim 1, and further comprising: thickening the waste activated sludge by removing filtrate prior to supplying the waste activated sludge through the heat exchanger to the thermophilic digester. ### Claim 5 (depends on 4) The waste treatment process of claim 4, wherein the filtrate is supplied to the struvite reactor. ### Claim 6 (depends on 5) The waste treatment process of claim 5, and further comprising: dewatering the mesophilic digestate prior to supplying a mesophilic effluent to the struvite reactor. ### Claim 7 (depends on 6) The waste treatment process of claim 6, wherein separating struvite comprises: settling struvite in the struvite reactor. ### Claim 8 (depends on 7) The waste treatment process of claim 7 wherein separating struvite further comprises: separating, with a cyclone separator, additional struvite fines remaining suspended in treated effluent from the struvite reactor. ### Claim 9 (depends on 1) The waste treatment process of claim 1, wherein increasing the pH comprises: removing carbon dioxide from the thermophilic digestate. ### Claim 10 (depends on 9) The waste treatment process of claim 9, wherein removing carbon dioxide from the thermophilic digestate comprises: supplying air to a coarse bubble air diffuser; and passing air bubbles through the thermophilic digestate. ### Claim 11 (depends on 1) The waste treatment process of claim 1, wherein increasing pH of the thermophilic digestate comprises: adding a reagent to the thermophilic digestate to increase pH. ### Claim 12 A waste treatment process comprising: processing waste activated sludge (WAS) in a thermophilic digester to produce a thermophilic digestate; increasing pH of the thermophilic digestate with an air stripper/heat exchanger subsequent to the thermophilic digester; forming struvite in the air stripper/heat exchanger to reduce a limiting element of struvite formation from the thermophilic digestate, thereby reducing struvite scaling on downstream equipment; cooling the thermophilic digestate concurrently with increasing pH of the thermophilic digestate in the air stripper/heat exchanger; producing from the thermophilic digestate that has been increased in pH and cooled, a treated digestate containing struvite with a struvite reactor; separating struvite from the treated digestate, subsequent to separating struvite from the treated digestate, processing the treated digestate in a mesophilic digester to produce a mesophilic digestate; and dewatering the mesophilic digestate to produce effluent and solids. ### Claim 13 A waste treatment system comprising: a thermophilic digester that produces a thermophilic digestate from waste activated sludge; an air stripper/heat exchanger, downstream of the thermophilic digester, that is fed a thermophilic digestate from the thermophilic digester and concurrently removes carbon dioxide from the thermophilic digestate to increase pH of the thermophilic digestate to reduce struvite scaling on downstream equipment and cools the thermophilic digestate by heat transfer from thermophilic digester to the waste activated sludge; a mesophilic digester, downstream of the air stripper/heat exchanger, that produces a mesophilic digestate from pH increased and cooled thermophilic digestate; a struvite reactor that produces a treated digestate containing struvite from the mesophilic digestate; and a pump downstream from the struvite reactor that supplies the mesophilic digestate to a cyclone separator to separate struvite from the mesophilic digestate. ### Claim 14 (depends on 13) The waste treatment system of claim 13, wherein the air stripper/heat exchanger includes a chamber, a coarse bubble air diffuser, an air pump or blower, and a sleeve or jacket. ### Claim 15 (depends on 13) The waste treatment system of claim 13, wherein the air stripper/heat exchanger and the struvite reactor are upstream of the mesophilic digester. ### Claim 16 A waste treatment process comprising: supplying waste activated sludge through a heat exchanger to a thermophilic digester; processing the waste activated sludge received from the heat exchanger in a thermophilic digester to produce a thermophilic digestate; increasing pH of the thermophilic digestate downstream of the thermophilic digester prior to any other processing; forming struvite concurrently with increasing pH of the thermophilic digestate to reduce a limiting element of struvite formation from the thermophilic digestate and to reduce struvite scaling on downstream equipment; subsequent to increasing pH of the thermophilic digestate and prior to any other processing, cooling the thermophilic digestate in the heat exchanger by heat transfer from the thermophilic digestate to the waste activated sludge; processing the pH increased and cooled thermophilic digestate in a mesophilic digester downstream of the heat exchanger and prior to any other processing to produce a mesophilic digestate; producing, with a struvite reactor, a treated digestate containing struvite; and separating struvite from the treated digestate with a cyclone supplied by a pump. ### Claim 17 (depends on 16) The waste treatment process of claim 16, wherein separating struvite comprises: dewatering treated digestate from the struvite reactor to separate effluent and biosolids enriched with struvite. ### Claim 18 (depends on 17) The waste treatment process of claim 17, wherein separating struvite further comprises: separating struvite with a cyclone separator supplied by a pump from the treated digestate prior to dewatering. ### Claim 19 (depends on 16) The waste treatment process of claim 16, and further comprising: thickening the waste activated sludge by removing filtrate prior to supplying the waste activated sludge through the heat exchanger to the thermophilic digester. ### Claim 20 (depends on 19) The waste treatment process of claim 19, wherein the filtrate is supplied to the struvite reactor. ### Claim 21 (depends on 20) The waste treatment process of claim 20 wherein separating struvite comprises: separating, with a cyclone separator supplied by a pump, struvite fines suspended in treated effluent from the struvite reactor and prior to any other dewatering. ### Claim 22 (depends on 16) The waste treatment process of claim 16, wherein increasing the pH comprises: removing carbon dioxide from the thermophilic digestate. ### Claim 23 (depends on 16) The waste treatment process of claim 16, wherein forming struvite concurrently with increasing the pH of the thermophilic digestate exhausts the limiting element of struvite formation. ### Claim 24 (depends on 12) The waste treatment process of claim 12, and further comprising: thickening the waste activated sludge by removing filtrate immediately prior to processing waste activated sludge in a thermophilic digester. ### Claim 25 (depends on 12) The waste treatment process of claim 12, and further comprising: Supplying waste activated sludge through a heat exchanger directly before processing waste activated sludge in a thermophilic digester. ### Claim 26 (depends on 12) The waste treatment process of claim 12, wherein separating struvite comprises: settling struvite in the struvite reactor; and separating, with a cyclone separator supplied by a pump, additional struvite fines remaining suspended in treated effluent from the struvite reactor.