Control of activated sludge wastewater treating process for enhanced phosphorous removal

• US 4,271,026 A
• Filed: 10/09/1979
• Issued: 06/02/1981
• Est. Priority Date: 10/09/1979
• Status: Expired due to Term

• Current Assignee: I. Kruger Inc. (Veolia Environnement SA)
• Original Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Inventors: Spector, Marshall L., Greskovich, Eugene J., Chen, Michael S.
• Primary Examiner(s): Wyse, Thomas G.
• Application Number:
  US06/083,196
• Time in Patent Office: 602 Days
• Field of Search: 210/DIG. 28, 210/DIG. 29, 210/605, 210/614, 210/623, 210/626, 210/630, 210/631, 210/903, 210/906
• US Class Current: 210/605
• CPC Class Codes: C02F 1/006 Water distributors either inside a treatment tank or directing the water to several treatment tanks; Water treatment plants incorporating these distributors, with or without chemical or biological tanks for settling tanks B01D21/24
• CPC Class Codes: C02F 3/1215 Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/903 Nitrogenous
• CPC Class Codes: Y10S 210/906 Phosphorus containing

Abstract

An improved method of operating an activated biomass process wherein influent and activated biomass are initially contacted under anaerobic conditions to form a mixed liquor, the mixed liquor is subsequently oxygenated, thereafter activated biomass is separated from the mixed liquor and at least a portion of the separated biomass is introduced into the initial contacting step. The improved method comprises maintaining both the F/M ratio and the BOD/P ratio within particular ranges, preferably relative to each other.

Claims

1. In an activated biomass process which inhibits the proliferation of filamentous biomass and effects the storage of phosphates in the biomass by first mixing recycled activated biomass with a phosphate- and BOD-containing influent to form a mixed liquor having both liquid and solid components and initially treating the mixed liquor under anaerobic conditions such as to be substantially free of oxygen and oxidizing agents and to contain a concentration of less than about 0.7 ppm dissolved oxygen;

thereby effecting selective production of nonfilamentous microorganisms capable of sorbing BOD under both anaerobic and oxidizing conditions and capable of accumulating phsophates under oxidizing conditions;

subjecting the anaerobically treated mixed liquor to a subsequent oxygenating treatment by contact with oxygen-containing gas admitted to said treatment under oxic conditions such as to have maintained in the treatment a dissolved oxygen content of at least about 1 ppm to oxidize BOD in the mixed liquor to cause further removal of BOD from the liquid component and to cause accumulation of phosphates in the solid biomass component;

subsequently separating the oxically treated mixed liquor into supernatant liquid and biomass; and

returning a portion of the separated biomass to an initial anaerobic treatment to provide the activated biomass admixed therein with the influent;

the improvement which comprises maintaning within the process system encompassing the initial anaerobic treatment and extending through the process up to, but not including, the separating step and including any internal recycle streams, a BOD₅ to phosphorous (BOD/P) ratio from about 5;

1 up to about 50;

1, wherein BOD₅ is expressed as milligrams of soluble BOD₅, exclusive of BOD attributable to ammonia, per liter of influent and P is soluble phosphate expressed as milligrams of elemental phosphorous per liter of influent, and a food to biomass (F/M) ratio from about 0.09 up to an upper limit of about 1.4 wherein F is the total weight of soluble BOD₅ introduced into the process per 24 hour day, and M is the weight of volatile suspended solids in the process system.

2. The process of claim 1 wherein the F/M ratio is at least about 0.1.

3. The process of claim 1 wherein the F/M ratio is less than about 1.0.

4. The process of claim 1 wherein the BOD/P ratio is from about 5:

1 up to about 10;

1 and the F/M ratio is less than about 0.6.

5. The process of claim 4 wherein the F/M ratio is less than about 0.3.

6. The process of claim 1 wherein the BOD/P ratio is from about 10:

1 to about 20;

1 and the F/M ratio is less than about 1.0.

7. The process of claim 6 wherein the F/M ratio is less than about 0.45.

8. The process of claim 1 wherein the BOD/P ratio is from about 20:

1 to about 50;

1 and the F/M ratio is less than about 1.4.

9. The process of claim 8 wherein the F/M ratio is less than about 0.5.

10. The process of claim 1 wherein the influent further contains ammonia values which are oxidized to nitrates and/or nitrites in an oxic treatment and wherein the mixed liquor initially treated under anaerobic conditions is further treated under anoxic conditions;

the anoxic conditions including being substantially free of oxygen and oxidizing agents and having a dissolved oxygen content of less than about 0.7 ppm and wherein nitrates and/or nitrites are introduced to the anoxic treatment by transfer to said treatment of mixed liquor from an oxic treatment, said oxygenated mixed liquor having a concentration of nitrites and/or nitrates in excess of 2 ppm, expressed as elemental nitrogen, and the nitrites and/or nitrates being reduced in the anoxic treatment to elemental nitrogen gas.

11. The process of claim 10 wherein the F/M ratio is at least about 0.10 but is less than about 0.75.

12. The process of claim 10 wherein the BOD/P ratio is from about 5:

1 up to about 10;

1 and the F/M ratio is less than about 0.3.

13. The process of claim 10 wherein the BOD/P ratio is from about 10:

1 up to about 20;

1 and the F/M ratio is less than about 0.45.

14. The process of claim 10 wherein the BOD/P ratio is from about 20:

1 up to about 50;

1 and the F/M ratio is less than about 0.5.

15. The process of claim 1 wherein the F/M ratio and the BOD/P ratio are maintained within the recited limits by controlling at least one of the amount of BOD introduced into the system, the amount of phosphorous introduced into the system and the recycle rate of activated biomass.

16. The process of claim 1 wherein the BOD/P ratio is controlled by chemically reducing the phosphorous in the system.

17. The process of claim 1 which is a fermentation process in which a desired material is contained in the supernatant liquid and the supernatant liquid is recovered as product.

18. The process of claim 1 wherein the F/M ratio is controlled in an existing treating system by eliminating from the process system a portion of the volume of an existing treating basin.

19. The improvement of claim 1 which further includes controlling the Influent Detention Time (IDT) of the anaerobic treatment and of the oxic treatment such that the IDT of the anaerobic treatment is from about 5% to about 80% of the total IDT of the process system, and the IDT of the oxic treatment is from about 95% to about 20% of the total IDT of the process system.

20. The improvement of claim 19 wherein the IDT of the anaerobic treatment is from about 10% to about 70% of the total IDT and the IDT of the oxic treatment is from about 90% to about 30% of the total IDT.

21. The improvement of claim 19 wherein the IDT of the anaerobic treatment is from about 20% to about 60% of the total IDT and the IDT of the oxic treatment is from about 80% to about 40% of the total IDT.

22. The improvement of claim 10 which further includes controlling the IDT of the anaerobic treatment, of the oxic treatment and of the anoxic treatment such that the IDT of the anaerobic treatment is from about 5% to about 80% of the total IDT of the process system, the IDT of the oxic treatment is from about 20% to about 95% of the total IDT of the process system and the IDT of the anoxic treatment is from about 5% to about 50% of the total IDT of the process sytem.

23. The improvement of claim 22 wherein the IDT of the anoxic treatment is from about 5% to about 30% of the total IDT of the process system.

24. The improvement of claim 22 wherein the IDT of the anoxic treatment is from about 10% to about 20% of the total IDT of the process system.

25. The improvement of claim 1 which further includes controlling the IDT of the anaerobic and oxic treatments such that, of the total IDT of the anaerobic and oxic treatments, the IDT of the anaerobic treatment is from about 10% to about 70% of such total IDT and the IDT of oxic treatment is from about 90% to about 30% of such total.

26. The improvement of claim 25 wherein the IDT of the anaerobic treatment is from about 10% to about 60% of such total IDT and the IDT of the oxic treatment is from about 90% to about 40% of such total.