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US4352738A Expired / Lapsed US ⏱️ 0.0 years remaining

Anaerobic filter

Assignee: Celanese International Corp
•
Filing: 1980-11-10
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Granted: 1982-10-05
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Expires: 2000-11-10
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Abstract

Abstract In the operation of a recycling anaerobic filter for treating aqueous waste streams, the rate of production of methane is measured continually at frequent intervals and the COD feed rate is varied to maintain a predetermined, timed, relationship between that varied feed rate and the measured methane production rate.

Inventors

  • 👤 George A. Blay
  • 👤 Enrique R. Witt

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 23:56
CPC Classifications
G; G05; G05D; G05D21/00; G05D21/02; C; C02; C02F; C02F3/00; C02F3/006; C02F3/28; C02F3/2806; C12; C12M; C12M21/00; C12M21/04; C12M41/00; C12M41/30; C12M41/34; C12M41/36; Y; Y02; Y02E; Y02E50/00; Y02E50/30

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 163 words
Process for the treatment of an organic wastewater stream containing COD in a recycling anaerobic filter which contains methanogenic bacteria, operates at a COD feed rate, OL, which is at least 0.5 lb COD/cu. ft./day, and produces a stream of gas comprising methane, wherein the improvement comprises continually carrying out an alternating sequence of steps at least once per four hour period, the steps of said sequence comprising, (a) a step of measuring the rate of production of methane in said gas stream and thereby determining the rate, KL, at which COD is removed from said filter as methane, and (b) a step of setting the COD feed rate, OL, to said filter to maintain a predetermined ratio between the KL determined in said step a and the OL set in said step b, said predetermined ratio of KL to OL, both KL and OL being expressed in the same units of lbs. COD/cu. ft./day, having a value of about 0.65 to 0.9.
Claim 2
Dependent Claim 163 words
Process for the treatment of an organic wastewater stream containing COD in a recycling anaerobic filter which contains methanogenic bacteria, operates at a COD feed rate, OL, which is at least 0.5 lb COD/cu. ft./day, and produces a stream of gas comprising methane, wherein the improvement comprises continually carrying out an alternating sequence of steps at least once per four hour period, the steps of said sequence comprising, (a) a step of measuring the rate of production of methane in said gas stream and thereby determining the rate, KL, at which COD is removed from said filter as methane, and (b) a step of setting the COD feed rate, OL, to said filter to maintain a predetermined ratio between the KL determined in said step a and the OL set in said step b, said predetermined ratio of KL to OL, both KL and OL being expressed in the same units of lbs. COD/cu. ft./day, having a value of about 0.65 to 0.9.
Claim 3
Dependent Claim 24 words
Process as in claim 1 and including the step of feeding the outfall of said recycling anaerobic filter directly to a second anaerobic filter.
Claim 4
Dependent Claim 30 words
Process as in claim 2 in which said waste stream is heated in said recycling anaerobic filter and said outfall is fed, in thus-heated condition, directly to said second filter.
Claim 5
Dependent Claim 19 words
Process as in claim 1 in which said sequence of steps is carried out at least once per hour.
Claim 6
Dependent Claim 25 words
Process as in claim 4 in which said alternating sequence is effected so frequently that the magnitudes of OL changes are each less than 10%.
Claim 7
Dependent Claim 20 words
Process as in claim 1 in which said sequence of steps is carried out at least once per 15-minute period.
Claim 8
Dependent Claim 28 words
Process as in claim 1 in which the KL is increased, by carrying out said alternating sequence continually, to a value of at least 1.5 lb. COD/cu. ft./day.
Claim 9
Dependent Claim 47 words
Process as in claim 1 in which, by carrying out said alternating sequence continually, the amount of biomass in said filter is raised to such a level that the amount of free liquid in said filter is less than 70% of the void volume of the filter
Claim 10
Dependent Claim 20 words
Process as in claim 8 in which said amount of free liquid is less than 50% of said void volume.

References Cited (Backward Citations)

DE2520742A1 Cited
US4182675A Cited
US4134830A Cited
US4145279A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-10-04 1986-04-05 1986-10-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-10-04 1990-04-05 1990-10-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-10-04 1994-04-05 1994-10-05 $7700.00 Window Closed / Lapsed

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