GB111401A - Improvements in the Treatment of Sewage for the Purification thereof and the Production of Combustible Gas therefrom. - Google Patents

Improvements in the Treatment of Sewage for the Purification thereof and the Production of Combustible Gas therefrom.

Info

Publication number
GB111401A
GB111401A GB289317A GB289317A GB111401A GB 111401 A GB111401 A GB 111401A GB 289317 A GB289317 A GB 289317A GB 289317 A GB289317 A GB 289317A GB 111401 A GB111401 A GB 111401A
Authority
GB
United Kingdom
Prior art keywords
sewage
tank
pipe
effluent
chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB289317A
Inventor
Horace Flicker
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to GB289317A priority Critical patent/GB111401A/en
Publication of GB111401A publication Critical patent/GB111401A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/24Activated sludge processes using free-fall aeration or spraying
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

111,401. Flicker, H. Feb. 27, 1917. Aerating; plant.-A process for purifying sewage comprises charging it with air, introducing the aerated sewage over the surface of sewage contained in a tank, the downward movement of the sewage in the tank while it is subjected to bacterial resolution, the continuous discharge of the effluent, and the periodical withdrawal of sludge. The combustible gases evolved may be collected for heating and lighting purposes. In the plant shown in Fig. 2, an aerating-device 2 charges the inflowing sewage in the pipe 1 with air, and the aerated sewage is sprayed by sprinklers 3 over the surface of the sewage in a chamber 5 formed by the wall of the tank and a baffle 7. The effluent leaves the chamber 5 by a passage 6, passes across the surface of the sludge deposited in a chamber 8 so as to facilitate the liberation of gas therefrom, and leaves the tank by a passage 9 and over a sill 11 where it is broken up to facilitate the liberation of gas from it. The leaving effluent is further aerated at 106. When the sludge reaches a gutter 14, as determined by the aid of a test pipe 105, some of it is drawn off by a pipe 101. Spray pipes 104, 102 facilitate cleansing the bottom of the tank and the pipe 101. The lower edges of the baffles are serrated to provide even distribution of the effluent. Gas may be drawn off by a pipe 20, and some of it is utilized in a heater 23 from which hot fluid is passed through a coil 24 in the tank to maintain the sewage at a temperature suited to the bacterial action. A circular tank is similarly arranged, annular baffles and a central discharge pipe being provided. In the circular tank shown in Fig. 4, the aerated sewage is supplied by sprinklers 304. The effluent flows downward in a chamber 302 and under a baffle 305 to an outlet 313, while the sludge is collected in a central chamber 308.
GB289317A 1917-02-27 1917-02-27 Improvements in the Treatment of Sewage for the Purification thereof and the Production of Combustible Gas therefrom. Expired GB111401A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB289317A GB111401A (en) 1917-02-27 1917-02-27 Improvements in the Treatment of Sewage for the Purification thereof and the Production of Combustible Gas therefrom.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB289317A GB111401A (en) 1917-02-27 1917-02-27 Improvements in the Treatment of Sewage for the Purification thereof and the Production of Combustible Gas therefrom.

Publications (1)

Publication Number Publication Date
GB111401A true GB111401A (en) 1917-11-29

Family

ID=32244047

Family Applications (1)

Application Number Title Priority Date Filing Date
GB289317A Expired GB111401A (en) 1917-02-27 1917-02-27 Improvements in the Treatment of Sewage for the Purification thereof and the Production of Combustible Gas therefrom.

Country Status (1)

Country Link
GB (1) GB111401A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0028050A1 (en) * 1979-10-26 1981-05-06 Stork Amsterdam B.V. Reactor for anaerobic fermentation of waste water
EP0143149A1 (en) * 1983-09-29 1985-06-05 Abwasserverband Raumschaft Lahr Method for the reduction of the H2S content in processes of anaerobic decomposition, especially in sludge digestion
EP0153299A1 (en) * 1984-02-14 1985-08-28 Nöbl, Ernst Dipl.Ing. Process and plant for the anaerobic treatment of organic substrates

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0028050A1 (en) * 1979-10-26 1981-05-06 Stork Amsterdam B.V. Reactor for anaerobic fermentation of waste water
US4346000A (en) 1979-10-26 1982-08-24 Stork Amsterdam B.V. Reactor for anaerobic prefermentation of aqueous waste waters
EP0143149A1 (en) * 1983-09-29 1985-06-05 Abwasserverband Raumschaft Lahr Method for the reduction of the H2S content in processes of anaerobic decomposition, especially in sludge digestion
EP0153299A1 (en) * 1984-02-14 1985-08-28 Nöbl, Ernst Dipl.Ing. Process and plant for the anaerobic treatment of organic substrates
WO1985003695A1 (en) * 1984-02-14 1985-08-29 Noebl Ernst Process and plant for the anaerobic treatment of organic substrates
US4746433A (en) * 1984-02-14 1988-05-24 Ernst Nobl Process for the anaerobic treatment of organic substrates

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