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US4122013A Expired / Lapsed US ⏱️ 0.0 years remaining

Sewage treatment system

Assignee: RESOURCES UTILITIES SYSTEMS CORP MANOR 504 CHESTNUT HILL VILLAGE PHILADELPHIA PA 19118 A CORP OF PA
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Filing: 1977-11-15
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Granted: 1978-10-24
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Expires: 1997-11-15
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Abstract

Abstract A sewage treatment system is divided into two stages with a collection system dispersed therebetween. The first stage includes anoxic treatment units producing an anaerobic effluent which is moved through the vacuum tight collection system to the second stage of treatment including an oxidation unit producing an aerobic effluent containing nitrates, dissolved oxygen and activated sludge. The two liquids are mixed in a chamber and are subjected to treatment before discharge for producing a highly treated effluent from which a major part of the nutrients have been removed.

Inventors

  • 👤 John W. Greenleaf, Jr.
  • 👤 Harold E. Schmidt

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 19:33
CPC Classifications
C; C02; C02F; C02F3/00; C02F3/02; C02F3/12; C02F3/1236; C02F3/1242; C02F3/30; C02F3/302; Y; Y02; Y02W; Y02W10/00; Y02W10/10

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 522 words
A sewage transport and treatment system, comprising a first sewage treatment station including an anoxic unit having first and second compartment with removable covers, said first compartment having an inlet for receiving residential or commercial sewage and having upper and lower portions for respectively accumulating scum and settleable solids, said compartments being separated by means of a vertical partition having ports near the bottom thereof for the passage of settled sewage into said second compartment, an outlet on said second compartment, a coarse media filling said second compartment to provide a large surface area for the attachment of anaerobic slime, said media defining free flowing spaces in the interstices thereof to provide intimate and prolonged contact of the settled sewage on its passage through said unit to said outlet whereby the treated sewage is anaerobically stabilized before its conveyance through the transport system, a vacuum transport system for collecting the anaerobically stabilized sewage from the first sewage treatment station and delivering it to a second sewage treatment station, the second sewage treatment station including a mixing tank for mixing the anaerobically stabilized sewage with pumped recirculated oxidation tank effluent containing dissolved oxygen and activated sludge under pressure, an open equilization tank for receiving discharge from said mixing tank and being fluidly interconnected therewith, a float control outlet valve on said equalization tank including a float disposed in a flow control chamber for maintaining a constant level of the discharge in said chamber, an outlet on said chamber controlled by an adjustable gate valve for controlling the rate of flow of the discharge, an oxidation tank having an air distribution manifold and a compressor for aerating and mixing the contents thereof, said oxidation tank being located below said control chamber and having an outlet weir extending the length thereof, a filter tank fluidly connected to said oxidation tank for filtering out activated sludge for the effluent, said filter tank including a pair of upflow filter units containing filter media and independent compartments lying therebeneath for accumulating activated sludge from the effluent passing upwardly therethrough, piping for conducting the discharge from said outlet weir to said compartments and further piping to return the discharge containing both dissolved oxygen and activated sludge from said compartments at a constant rate through a pump to said mixing tank to be mixed with incoming anaerobically treated sewage and reintroduced into said second station, said filter units serving to filter aerobically treated sewage in excess of that recirculated through the mixing tank and aerobic treatment system at the rate of flow established at said control chamber, said filter tank including a chlorine contact chamber located above said filter units for effluent sterilization, said rate of flow establishing a discharge rate and a detention time in said chamber which is provided for the disinfection of the plant effluent before discharge, a constant head tank having distributing means extending into said contact chamber, and including a float valve control and a valve outlet for determining the rate of flow of disinfecting solution from a storage tank fluidly connected therewith, and means for backwashing the filter units to remove sludge accumulation therefrom.
Claim 2
Dependent Claim 522 words
A sewage transport and treatment system, comprising a first sewage treatment station including an anoxic unit having first and second compartment with removable covers, said first compartment having an inlet for receiving residential or commercial sewage and having upper and lower portions for respectively accumulating scum and settleable solids, said compartments being separated by means of a vertical partition having ports near the bottom thereof for the passage of settled sewage into said second compartment, an outlet on said second compartment, a coarse media filling said second compartment to provide a large surface area for the attachment of anaerobic slime, said media defining free flowing spaces in the interstices thereof to provide intimate and prolonged contact of the settled sewage on its passage through said unit to said outlet whereby the treated sewage is anaerobically stabilized before its conveyance through the transport system, a vacuum transport system for collecting the anaerobically stabilized sewage from the first sewage treatment station and delivering it to a second sewage treatment station, the second sewage treatment station including a mixing tank for mixing the anaerobically stabilized sewage with pumped recirculated oxidation tank effluent containing dissolved oxygen and activated sludge under pressure, an open equilization tank for receiving discharge from said mixing tank and being fluidly interconnected therewith, a float control outlet valve on said equalization tank including a float disposed in a flow control chamber for maintaining a constant level of the discharge in said chamber, an outlet on said chamber controlled by an adjustable gate valve for controlling the rate of flow of the discharge, an oxidation tank having an air distribution manifold and a compressor for aerating and mixing the contents thereof, said oxidation tank being located below said control chamber and having an outlet weir extending the length thereof, a filter tank fluidly connected to said oxidation tank for filtering out activated sludge for the effluent, said filter tank including a pair of upflow filter units containing filter media and independent compartments lying therebeneath for accumulating activated sludge from the effluent passing upwardly therethrough, piping for conducting the discharge from said outlet weir to said compartments and further piping to return the discharge containing both dissolved oxygen and activated sludge from said compartments at a constant rate through a pump to said mixing tank to be mixed with incoming anaerobically treated sewage and reintroduced into said second station, said filter units serving to filter aerobically treated sewage in excess of that recirculated through the mixing tank and aerobic treatment system at the rate of flow established at said control chamber, said filter tank including a chlorine contact chamber located above said filter units for effluent sterilization, said rate of flow establishing a discharge rate and a detention time in said chamber which is provided for the disinfection of the plant effluent before discharge, a constant head tank having distributing means extending into said contact chamber, and including a float valve control and a valve outlet for determining the rate of flow of disinfecting solution from a storage tank fluidly connected therewith, and means for backwashing the filter units to remove sludge accumulation therefrom.

References Cited (Backward Citations)

US3228531A Cited
US3166501A Cited
FR1402406A Cited
US3306447A Cited
US3666106A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-10-23 1982-04-24 1982-10-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-10-23 1986-04-24 1986-10-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-10-23 1990-04-24 1990-10-24 $7700.00 Window Closed / Lapsed

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