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Anaerobic filter
| Details |
Inventors: Blay, George A.; Witt, Enrique R.;
Assignee: Celanese Corporation (New York, NY)
Primary Examiner:
Assistant Examiner:
Attorney, Agent or Firm:
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. |
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DETAILED DESCRIPTION The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows: 1. Process for the treatment of an organic waste-water 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 at a recycle ratio of at least 2:1, and produces a stream of gas comprising methane, wherein the improvement comprises continually carrying out an alternating sequence of steps at least once per hour, 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, in lbs. COD/cu. ft. /day, to said filter at a numerical value which is larger than the KL, in lbs. COD/cu. ft. /day, determined in said step a and which is related to said KL according to a predetermined mathematical formula, the numerical value of OL set in each step b of said sequence being related by the same predetermined formula to the respective value of KL determined in the corresponding preceding step a of said sequence, said recycle ratio being the ratio of the volumetric flow rate of the recycled liquid to the volumetric flow rate of the fresh feed. 2. Process as in claim 1 in which said sequence of steps is carried out at least once per 15-minute period. 3. Process as in claim 1 in which said alternating sequence is effected so frequently that the magnitudes of OL changes are each less than 10%, and in which the recycle ratio is at least about 4:1 and less than 15:1. 4. Process as in claim 3 in which the formula is (KL/OL)=C where C is a constant. 5. Process as in claim 1 in which the formula is: OL-KL=C where C is a constant. 6. Process as in claim 1 in which the formula is (KL/OL)=C where C is a constant. 7. Process as in claim 6 in which C is less than 0. 9. 8. Process as in claim 1 in which said alternating sequence is followed by another alternating sequence according to claim 1, the mathematical formula for the latter sequence being different from that of the former sequence
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