# US 11,299,415 B2 · Dissolved air flotation system and methods for biological nutrient removal > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,299,415 B2 - Document ID: US11299415B2 - Status: Granted - Kind: B2 - Application number: 16/979,855 - Filed: 2019-03-12 - Published: 2021-02-18 - Granted: 2022-04-12 - Earliest claimed: 2018-03-12 - Assignees: Evoqua Water Technologies LLC - Applicants: Evoqua Water Technologies LLC - Inventors: Nathan Antonneau - Web page: https://patentgrep.com/patent/US11299415B2 ## CPC - C02F 9/00: Multistage treatment of water, waste water or sewage - C02F 1/001: {Processes for the treatment of water whereby the filtration technique is of importance (C02F1/44 takes precedence; construction of filters in general B01D24/00 - B01D41/00)} - C02F 1/24: by flotation (C02F1/465 takes precedence) - C02F 1/5245: {using basic salts, e.g. of aluminium and iron} - C02F 3/12: Activated sludge processes - C02F 3/1278: {Provisions for mixing or aeration of the mixed liquor} - C02F 3/28: Anaerobic digestion processes - C02F 3/308: {Biological phosphorus removal} - C02F 11/04: Anaerobic treatment; Production of methane by such processes - C02F 2101/105: {Phosphorus compounds} - C02F 2201/005: Valves - C02F 2203/002: comprising an initial buffer container - C02F 2203/004: comprising a selector reactor for promoting floc-forming or other bacteria - C02F 2209/08: Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD] - C02F 2209/10: Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS] - C02F 2209/18: PO4-P - C02F 2301/046: Recirculation with an external loop - C02F 2303/24: Separation of coarse particles, e.g. by using sieves or screens - Y02W 10/10: Biological treatment of water, waste water, or sewage - 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) - Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT ## Abstract A wastewater treatment system including a contact tank, a dissolved air flotation unit, a fermentation unit, and a biological treatment unit is disclosed. A method of retrofitting a wastewater treatment system by arranging the wastewater treatment system such that floated biosolids are fermented in an anerobic environment and fluidly connecting the biological treatment unit to receive at least a portion of the fermented solids is also disclosed. The method optionally includes providing a fermentation unit and fluidly connecting the fermentation unit to a biological treatment unit. A method of treating wastewater including combining the wastewater with activated sludge, floating biosolids from the activated wastewater, fermenting the floated biosolids, and biologically treating the effluent with the fermented solids is also disclosed. A method of facilitating delivery of soluble organic carbon to a biological treatment unit is also disclosed. ## Claims ### Claim 1 A wastewater treatment system comprising: a contact tank having a first inlet fluidly connectable to a source of wastewater to be treated, and an outlet, the contact tank configured to treat the wastewater with activated sludge to form a first mixed liquor; a dissolved air flotation unit having a first inlet fluidly connected to the outlet of the contact tank, a second inlet fluidly connected to a source of gas, a first floated solids outlet, a second floated solids outlet, and an effluent outlet, the dissolved air flotation unit configured to treat the first mixed liquor with the gas to form floated solids and an effluent; a fermentation unit having a first inlet fluidly connected to the first floated solids outlet, a first fermented solids outlet, and a second fermented solids outlet, the fermentation unit configured to treat at least a portion of the floated solids to form fermented solids; an anaerobic digester having a first inlet fluidly connected to the second floated solids outlet, a second inlet fluidly connected to the second fermented solids outlet, and an outlet; and a biological treatment unit having a first inlet fluidly connected to the effluent outlet, a second inlet fluidly connected to the first fermented solids outlet, and an outlet, the biological treatment unit configured to treat the effluent with at least a portion of the fermented solids to form a second mixed liquor. ### Claim 2 (depends on 1) The system of claim 1, wherein the contact tank has a second inlet and the biological treatment unit has a third inlet, the system further comprising: a solids-liquid separation unit having an inlet fluidly connected to the outlet of the biological treatment unit, a solids-lean effluent outlet, a first return activated sludge outlet fluidly connected to the second inlet of the contact tank, and a second return activated sludge outlet fluidly connected to the third inlet of the biological treatment unit, the solids-liquid separation unit configured to treat solids from the second mixed liquor to form a solids-lean effluent and return activated sludge. ### Claim 3 (depends on 1) The system of claim 1, further comprising a screen positioned between the first floated solids outlet and the first inlet of the fermentation unit, the screen configured to retain non-biological waste solids. ### Claim 4 (depends on 1) The system of claim 1, further comprising: a first metering valve positioned upstream from the first fermented solids outlet and the second fermented solids outlet; and a first controller operatively connected to the first metering valve and configured to instruct the first metering valve to selectively dispense the fermented solids to the biological treatment unit and to the anaerobic digester. ### Claim 5 (depends on 1) The system of claim 1, further comprising a screen positioned between the second floated solids outlet and the first inlet of the anaerobic digester, the screen configured to retain non-biological waste solids. ### Claim 6 (depends on 1) The system of claim 1, wherein the fermentation unit further comprises a third fermented solids outlet and the contact tank further comprises a third inlet fluidly connected to the third fermented solids outlet. ### Claim 7 (depends on 6) The system of claim 6, further comprising a screen positioned between the third fermented solids outlet and the third inlet of the contact tank, the screen configured to retain non-biological waste solids. ### Claim 8 (depends on 1) The system of claim 1, wherein the contact tank comprises a second outlet and the biological treatment unit comprises: an anaerobic region having a first inlet fluidly connected to the effluent outlet, and an outlet; an aerated anoxic region having a first inlet fluidly connected to the second outlet of the contact tank, a second inlet fluidly connected to the outlet of the anaerobic region, and an outlet; and an aerobic region having a first inlet fluidly connected to the outlet of the aerated anoxic region, a second inlet fluidly connected to the effluent outlet, and an outlet. ### Claim 9 (depends on 8) The system of claim 8, wherein at least one of the anaerobic region and the aerated anoxic region has an inlet fluidly connected to the first fermented solids outlet. ### Claim 10 (depends on 9) The system of claim 9, wherein the anaerobic region has a second inlet fluidly connected to the first fermented solids outlet and the aerated anoxic region has a third inlet fluidly connected to the first fermented solids outlet, the system further comprising: a second metering valve positioned downstream from the first fermented solids outlet; and and a second controller operatively connected to the second metering valve and configured to instruct the second metering valve to selectively dispense the fermented solids to the anaerobic region and to the aerated anoxic region. ### Claim 11 (depends on 8) The system of claim 8, wherein the biological treatment unit further comprises a post-anoxic region having a first inlet fluidly connected to the outlet of the aerobic region, a second inlet fluidly connected to the first fermented solids outlet, and an outlet. ### Claim 12 A method of treating wastewater comprising: directing the wastewater into a contact tank and mixing the wastewater with an activated sludge to form an activated mixed liquor; directing the activated mixed liquor into a dissolved air flotation unit and separating the activated mixed liquor to form a floated biosolids and an effluent; selectively directing a first portion of the floated biosolids into a fermentation unit and a second portion of the floated biosolids into an anaerobic digester, and fermenting the first portion of the floated biosolids in the fermentation unit to form a fermented solids; directing the effluent to a biological treatment unit; and selectively directing a first portion of the fermented solids into the biological treatment unit and a second portion of the fermented solids into the anaerobic digester, an amount of the first portion of the fermented solids directed into the biological treatment unit being selected responsive to a determination of a required soluble chemical oxygen demand of the biological treatment unit, and biologically treating the effluent with the first portion of the fermented solids in the biological treatment unit to form a biologically treated mixed liquor. ### Claim 13 (depends on 12) The method of claim 12, further comprising: directing the biologically treated mixed liquor into a solids-liquid separation unit and separating the biologically treated mixed liquor to form a solids-lean effluent and the activated sludge; directing a first portion of the activated sludge into the contact tank; and directing a second portion of the activated sludge into the biological treatment unit. ### Claim 14 (depends on 12) The method of claim 12, further comprising separating non-biological waste solids from at least one of the first portion of the floated biosolids and the second portion of the floated biosolids. ### Claim 15 (depends on 12) The method of claim 12, further comprising directing a third portion of the fermented solids into the contact tank. ### Claim 16 (depends on 15) The method of claim 15, further comprising separating non-biological waste solids from the third portion of the fermented solids. ### Claim 17 (depends on 12) The method of claim 12, wherein the first portion of the fermented solids is selectively directed into at least one of an anaerobic region, an aerated anoxic region, and a post-anoxic region of the biological treatment unit. ### Claim 18 (depends on 12) The method of claim 12, wherein treating the effluent with the first portion of the fermented solids comprises reducing a concentration of dissolved phosphorous in the effluent when forming the biologically treated mixed liquor. ### Claim 19 A wastewater treatment system comprising: a contact tank having a first inlet fluidly connectable to a source of wastewater to be treated, a first outlet, and a second outlet, the contact tank configured to treat the wastewater with activated sludge to form a first mixed liquor; a dissolved air flotation unit having a first inlet fluidly connected to the first outlet of the contact tank, a second inlet fluidly connected to a source of gas, a first floated solids outlet, and an effluent outlet, the dissolved air flotation unit configured to treat the first mixed liquor with the gas to form floated solids and an effluent; a fermentation unit having a first inlet fluidly connected to the first floated solids outlet, and a first fermented solids outlet, the fermentation unit configured to treat at least a portion of the floated solids to form fermented solids; and a biological treatment unit including: an anaerobic region having a first inlet fluidly connected to the effluent outlet, and an outlet; an aerated anoxic region having a first inlet fluidly connected to the second outlet of the contact tank, a second inlet fluidly connected to the outlet of the anaerobic region, and an outlet; an aerobic region having a first inlet fluidly connected to the outlet of the aerated anoxic region, a second inlet fluidly connected to the effluent outlet, and an outlet; a first inlet fluidly connected to the effluent outlet; a second inlet fluidly connected to the first fermented solids outlet; and an outlet, the biological treatment unit configured to treat the effluent with at least a portion of the fermented solids to form a second mixed liquor. ### Claim 20 A method of treating wastewater comprising: directing the wastewater into a contact tank and mixing the wastewater with an activated sludge to form an activated mixed liquor; directing the activated mixed liquor into a dissolved air flotation unit and separating the activated mixed liquor to form a floated biosolids and an effluent; selectively directing a first portion of the floated biosolids into a fermentation unit and a second portion of the floated biosolids into an anaerobic digester, and fermenting the first portion of the floated biosolids in the fermentation unit to form a fermented solids; directing the effluent to a biological treatment unit; and selectively directing a first portion of the fermented solids into the biological treatment unit and a second portion of the fermented solids into the anaerobic digester, and biologically treating the effluent with the first portion of the fermented solids in the biological treatment unit to form a biologically treated mixed liquor, treating the effluent with the first portion of the fermented solids comprising reducing a concentration of dissolved phosphorous in the effluent when forming the biologically treated mixed liquor.