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US4340484A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for the froth flotation separation and treatment of slowly biodegradable components in waste treatment

Assignee: Zeneca Corp
•
Filing: 1981-05-18
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Granted: 1982-07-20
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Expires: 2001-05-18
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Abstract

Abstract In a long vertical shaft bioreactor for the treatment of degradable wastes in a circulating loop, a process is provided for separating and treating the slowly biodegradable components of the waste. The process comprises the steps of aerating and oxidizing the waste liquor in the reactor to produce an effluent and a foam which foam contains the slowly biodegradable components, which have not been degraded in the oxidizing step, separating and collecting the foam, collapsing the foam and subjecting the collapsed foam to further aeration/oxidation treatment to produce a treated effluent. The thus further treated effluent is returned to the bioreactor for reprocessing.

Inventors

  • 👤 David C. I. Pollock
  • 👤 Malcolm A. Wilson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 15:33
CPC Classifications
C; C02; C02F; C02F3/00; C02F3/02; C02F3/12; C02F3/22; C02F3/226; C02F1/00; C02F1/24; Y; Y02; Y02W; Y02W10/00; Y02W10/10

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 293 words
In a modified activated sludge waste treatment method wherein an aerobic biological reaction takes place during the continuous circulation of fluid waste in an apparatus comprising a surface basin, a long vertical downcomer chamber, a long vertical riser chamber operatively communicating with the downcomer through the basin and at the lower end of the downcomer to form a circulating loop and including means to circulate waste liquor through said loop in the presence of oxygen-containing gas, the improvements whereby the slowly biodegradable components of the waste may be separated from the waste liquor in the loop, aerobically treated, and after treatment returned to the waste liquor in the loop, comprising the steps of: (a) introducing waste liquor from a single source into the said riser chamber of the said loop, (b) adding oxygen-containing gas to the waste liquor in the said riser chamber to lift said waste liquor for circulation through said loop and to provide oxygenation of the said waste, (c) collecting from the surface of said waste in the said surface basin any foam containing slowly biodegradable materials together with activated sludge, which foam has been produced by stripping the supersaturated dissolved gases ascending from depth in the said circulating loop by the action of the said added oxygen-containing gas in the said riser, (d) separating said foam and contained slowly biodegradable materials and activated sludge from the surface of the liquid waste in the said basin and transferring said foam and contained materials to a foam oxidation vessel, (e) aerating said foam in said foam oxidation vessel to produce further biodegraded liquid and solids mixture, and (f) returning the said further biodegraded liquids and solids mixture from step (e) to the circulating waste in the said loop via step (a).
Claim 2
Dependent Claim 293 words
In a modified activated sludge waste treatment method wherein an aerobic biological reaction takes place during the continuous circulation of fluid waste in an apparatus comprising a surface basin, a long vertical downcomer chamber, a long vertical riser chamber operatively communicating with the downcomer through the basin and at the lower end of the downcomer to form a circulating loop and including means to circulate waste liquor through said loop in the presence of oxygen-containing gas, the improvements whereby the slowly biodegradable components of the waste may be separated from the waste liquor in the loop, aerobically treated, and after treatment returned to the waste liquor in the loop, comprising the steps of: (a) introducing waste liquor from a single source into the said riser chamber of the said loop, (b) adding oxygen-containing gas to the waste liquor in the said riser chamber to lift said waste liquor for circulation through said loop and to provide oxygenation of the said waste, (c) collecting from the surface of said waste in the said surface basin any foam containing slowly biodegradable materials together with activated sludge, which foam has been produced by stripping the supersaturated dissolved gases ascending from depth in the said circulating loop by the action of the said added oxygen-containing gas in the said riser, (d) separating said foam and contained slowly biodegradable materials and activated sludge from the surface of the liquid waste in the said basin and transferring said foam and contained materials to a foam oxidation vessel, (e) aerating said foam in said foam oxidation vessel to produce further biodegraded liquid and solids mixture, and (f) returning the said further biodegraded liquids and solids mixture from step (e) to the circulating waste in the said loop via step (a).

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-07-19 1986-01-18 1986-07-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-07-19 1990-01-18 1990-07-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-07-19 1994-01-18 1994-07-20 $7700.00 Window Closed / Lapsed

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