Production of non-bulking activated sludge

Claim 2

In the operation of an activated sludge system the method of inhibiting proliferation of filamentous biomass consisting essentially of: producing a mixed liquor by mixing in an initial contact zone recycled activated sludge with BOD-containing wastewater influent; said initial contact zone being maintained under anaerobic conditions such as to be substantially free of NO x - and to contain a concentration of less than 0.7 ppm dissolved oxygen; thereby effecting selective production of nonfilamentous microorganisms capable of sorbing BOD; oxidizing BOD in the mixed liquor in a subsequent oxygenated zone to cause removal of BOD by contact with oxygen-containing gas admitted to said oxygenated zone, said oxygenated zone having maintained therein a dissolved oxygen content of at least 1 ppm; transferring the oxidized mixed liquor from said oxygenated zone to a settling zone wherein purified supernatant liquid is separated from settled sludge; and returning a portion of said settled sludge to said initial contact zone to provide the activated sludge admixed therein with the wastewater influent.

Claim 3

The method as defined in claim 1 wherein said initial contact zone comprises a series of at least two hydraulically distinct sections in concurrent liquid flow communication.

Claim 4

The method as defined in claim 2 wherein said distinct sections are physically separated by partitions.

Claim 5

The method as defined in claim 1 wherein said initial contact zone contains less than 0.4 ppm of dissolved oxygen.

Claim 6

The method as defined in claim 1 wherein said oxygenated zone comprises a series of at least two hydraulically distinct sections in concurrent liquid flow communication.

Claim 7

The method as defined in claim 5 wherein said distinct sections of said oxygenated zone are physically separated by partitions.

Claim 8

In the operation of an activated sludge system to effect biological removal of phosphates from influent wastewater while inhibiting proliferation of filamentous biomass, the method consisting essentially of: producing a mixed liquor by mixing in an initial contact zone recycled activated sludge with wastewater influent containing BOD and phosphates; said initial contact zone being maintained under anaerobic conditions such as to be substantially free of NO x - and to contain a concentration of less than 0.7 ppm dissolved oxygen; thereby effecting selective production of nonfilamentous microorganisms capable of sorbing BOD and capable of storing polyphosphate under oxidizing conditions; oxidizing BOD in the mixed liquor in a subsequent oxygenated zone to cause removal of BOD by contact with oxygen-containing gas addmitted to said oxygenated zone, thereby simultaneously effecting storage of phosphates within said microorganisms; said oxygenated zone having maintained therein a dissolved oxygen content of at least 1 ppm; transferring the oxidized mixed liquor from said oxygenated zone to a settling zone wherein purified supernatant liquid is separated from settled sludge; and returning a portion of said settled sludge to said initial contact zone to provide the activated sludge admixed therein with the wastewater influent.

Claim 9

In the operation of an activated sludge system to effect biological removal of phosphates from influent wastewater while inhibiting proliferation of filamentous biomass, the method consisting essentially of: producing a mixed liquor by mixing in an initial contact zone recycled activated sludge with wastewater influent containing BOD and phosphates; said initial contact zone being maintained under anaerobic conditions such as to be substantially free of NO x - and to contain a concentration of less than 0.7 ppm dissolved oxygen; thereby effecting selective production of nonfilamentous microorganisms capable of sorbing BOD and capable of storing polyphosphate under oxidizing conditions; oxidizing BOD in the mixed liquor in a subsequent oxygenated zone to cause removal of BOD by contact with oxygen-containing gas addmitted to said oxygenated zone, thereby simultaneously effecting storage of phosphates within said microorganisms; said oxygenated zone having maintained therein a dissolved oxygen content of at least 1 ppm; transferring the oxidized mixed liquor from said oxygenated zone to a settling zone wherein purified supernatant liquid is separated from settled sludge; and returning a portion of said settled sludge to said initial contact zone to provide the activated sludge admixed therein with the wastewater influent.

Claim 10

The method as defined in claim 7 wherein said initial contact zone comprises a series of at least two hydraulically distinct sections in concurrent liquid flow communication.

Claim 11

The method as defined in claim 8 wherein said distinct sections are physically separated by partitions.

Claim 12

The method as defined in claim 7 wherein said initial contact zone contains a total of less than 0.4 ppm dissolved oxygen.

Claim 13

The method as defined in claim 7 wherein nitrogen gas is contacted with mixed liquor in said initial contact zone to maintain anaerobic conditions therein.

Claim 14

The method of claim 7 where the biological sludge produced contains phosphate values in the order of up to 6%, expressed as elemental phosphorus on a dry basis, a portion of which is recovered for industrial use.

Claim 15

The method as defined in claim 7 wherein said wastewater influent further contains ammonia values and wherein the mixed liquor formed in said initial anaerobic contact zone is further treated in an anoxic zone under anoxic conditions before its being sent to the oxygenated zone; said anoxic conditions including a dissolved oxygen content not in excess of 0.7 ppm and the admission to said zone of nitrates and/or nitrites; said nitrates and/or nitrites being obtained by internal transfer of mixed liquor thereto from the oxygenated zone, said mixed liquor having a concentration of nitrates and/or nitrites in excess of 2 ppm, expressed as elemental nitrogen, and said nitrates and/or nitrites being reduced in said anoxic zone to elemental nitrogen gas.

Claim 16

The method as defined in claim 13 wherein said mixed liquor transferred from said oxygenated zone to said anoxic zone constitutes 100 to 400% by volume of the fresh wastewater influent admitted to said initial contact zone.

Claim 17

The method as defined in claim 13 wherein the sludge recycled to said initial contact zone constitutes 10 to 50% by volume of the fresh wastewater influent admitted to said initial contact zone.

Claim 18

The method as defined in claim 13 wherein said anoxic zone is comprised of a series of two or more sections in liquid flow communication.

Claim 19

The method as defined in claim 13 wherein the total influent detention time in said initial anaerobic contact zone, said anoxic zone and said aerating zone does not substantially exceed three hours.

Claim 20

The method as defined in claim 7 wherein the sludge recycled to said initial contact zone constitutes 10 to 50% by volume of the fresh wastewater influent admitted to said initial contact zone.

Claim 21

The method as defined in claim 7 wherein the total influent detention time in said initial anaerobic contact zone and said aerating zone does not substantially exceed three hours.