# US 5,344,562 A · Biological dephosphatization and (de)nitrification > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,344,562 A - Document ID: US5344562A - Status: Granted - Kind: A - Application number: 08/025,946 - Filed: 1993-03-03 - Granted: 1994-09-06 - Earliest claimed: 1987-02-27 - Inventors: Gunter Lorenz; Jurgen Lorenz - Web page: https://patentgrep.com/patent/US5344562A ## CPC - C02F 3/1215: {Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates} - C02F 3/308: {Biological phosphorus removal} - Y02W 10/10: Biological treatment of water, waste water, or sewage - Y10S 210/903: Nitrogenous - Y10S 210/906: Phosphorus containing - 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 - Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS ## Abstract A modified activated sludge system is provided wherein wastewater is treated to reduce BOD, nitrogen, and/or phosphorus. The disclosed system features a zone sequence nitrification/denitrification, with nitrification induced by recycling mixed liquor that contains a significant concentration of oxygen and nitrifying bacteria. With a further modification, the main treatment zones of the treatment system are split into two or more parallel treatment trains that are either high-loaded with BOD or low-loaded with BOD. The high-loaded sections facilitate the sludge generation and BOD removal, while the low-loaded sections are operated for nitrification and to enhance the growth of nitrifying bacteria. The parallel treatment zones combine and pass into a final denitrification zone. Phosphorus removal is achieved with phosphate release in a reverse flow regime to the main treatment, and phosphate retention primarily in aerated treatment zones in the main stream of the process. The phosphorus is discarded from the system as sludge. ## Claims ### Claim 1 An activated sludge process for the reclamation of wastewater, comprising the steps of: (a) separating incoming wastewater into two parallel streams; (b) nitrifying one of said parallel streams in a first treatment zone, thereby producing a nitrified effluent; (c) reducing the BOD in the other parallel stream by treatment in a second parallel treatment zone for BOD removal; (d) providing sufficient residence time for the waste-water in said two parallel treatment zones to effect sufficient growth of said bacteria; (e) extracting and disposing of sludge of said second treatment zone from step (c), thereby producing a clarified waste effluent stream; and (f) reuniting the nitrified effluent of step (b) with the clarified effluent from step (e) for further treatment of the wastewater. ### Claim 2 (depends on 1) The method as defined in claim 1, wherein said second parallel treatment zone comprises at least two hydraulically distinct sections in concurrent liquid flow communication followed by a sedimentation zone. ### Claim 3 (depends on 2) The method as defined in claim 2, wherein a portion of the treated wastewater is recycled from one said hydraulically distinct section to a preceding hydraulically distinct section of said second treatment zone. ### Claim 4 (depends on 2) The method as defined in claim 2, wherein a portion of the sedimented sludge is withdrawn from said sedimentation zone for digestion, the remainder being recycled to the first of said hydraulically distinct sections. ### Claim 5 (depends on 4) The method as defined in claim 4, wherein at least a portion of the digested sludge is recycled to the first of said hydraulically distinct sections. ### Claim 6 (depends on 2) The method as defined in claim 2, wherein at least a portion of the sedimented sludge withdrawn from said sedimentation zone is fed into a treatment zone following said two parallel treatment zones. ### Claim 7 (depends on 1) The method as defined in claim 1, wherein said first treatment zone comprises at least two hydraulically distinct sections in concurrent liquid flow communication. ### Claim 8 (depends on 7) The method as defined in claim 7, wherein the last of said hydraulically distinct sections is followed by a sedimentation zone, and wherein a portion of the settled sludge in said sedimentation zone is recycled to one of said two parallel treatment zones, the remainder being admitted to a zone before or after said parallel treatment zones. ### Claim 9 (depends on 8) The method as defined in claim 8, wherein said portion of the settled sludge passes through a digester before recycling to one of said two parallel treatment zones. ### Claim 10 (depends on 7) The method as defined in claim 7, wherein unsettled mixed liquor is recycled from one hydraulically distinct section to a preceding hydraulically distinct section. ### Claim 11 (depends on 1) The method as defined in claim 1, wherein the level of aeration of said second parallel treatment zone is determined by the desired level of phosphorus uptake. ### Claim 12 (depends on 1) The method as defined in claim 1, wherein the incoming wastewater passes through at least one initial treatment zone before entering said parallel treatment zones. ### Claim 13 (depends on 12) The method as defined in claim 12, wherein said initial treatment zones include a sludge settlement zone, feeding at least a portion of settled sludge of said sludge settlement zone into said second parallel treatment zone of step (c). ### Claim 14 (depends on 1) The method as defined in claim 1, wherein the BOD content of said first treatment zone is less than 0.6 kg BOD.sub.5 /(kg dry sludge * day), and wherein the BOD content of said second parallel treatment zone is greater than 0.6 kg BOD.sub.5 /(kg dry sludge * day).