Two-stage anaerobic/aerobic treatment process

• US 4,919,815 A
• Filed: 02/06/1989
• Issued: 04/24/1990
• Est. Priority Date: 02/06/1989
• Status: Expired due to Term

• Current Assignee: Siemens Water Technologies Corp (Siemens AG)
• Original Assignee: Zimpro Passavant Inc (Siemens AG)
• Inventors: Copa, William M., Vollstedt, Thomas J.
• Primary Examiner(s): Hruskoci, Peter
• Assistant Examiner(s): Upton, Christopher
• Application Number:
  US07/306,195
• Time in Patent Office: 442 Days
• Field of Search: 210/603, 210/605, 210/616, 210/623, 210/624, 210/631, 210/628, 210/617, 210/615, 210/630, 210/903
• US Class Current: 210/603
• CPC Class Codes: C02F 3/085 Fluidized beds
• CPC Class Codes: C02F 3/10 Packings; Fillings; Grids packing elements in general B01J19/30, B01J19/32
• CPC Class Codes: C02F 3/1263 Sequencing batch reactors [SBR]
• CPC Class Codes: C02F 3/2806 Anaerobic processes using solid supports for microorganisms
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

A two-stage process for purifying wastewater includes the steps of biophysical anaerobic treatment to remove the majority of the COD, followed by biophysical aerobic treatment to further purify the wastewater. A powdered adsorbent, preferably powdered activated carbon, is used with biological solids in each treatment step. Excess biophysical solids from the aerobic step are transferred to the anaerobic step for digestion. Fresh powdered adsorbent is added to the aerobic treatment step to compensate for that transferred to the anaerobic treatment step. Solids concentration in the anaerobic step is controlled by wasting solids to disposal.

Claims

1. A two-stage process for treating wastewater containing a COD of 5,000-50,000 mg/l comprising the steps;

(a) contacting said wastewater with anaerobic biosolids and powdered adsorbent in an anaerobic first treatment zone to form an anaerobic mixed liquor and remove a substantial portion of the COD from said wastewater;

(b) separating a fuel gas from said anaerobic mixed liquor within said first treatment zone;

(c) separating a substantial portion of the anaerobic biosolids and powdered adsorbent from said anaerobic mixed liquor by separating means within said first treatment zone to produce a first solids phase and a first aqueous phase;

(d) transferring said first aqueous phase from said first treatment zone to a second aerobic treatment zone.

(e) aerating and mixing said first aqueous phase with an oxygen-containing gas in said second treatment zone containing aerobic mixed liquor solids, composed of aerobic biosolids and powdered adsorbent, to remove a substantial portion of the remaining COD from said first aqueous phase;

(f) separating said aerobic mixed liquor solids from said thus-treated liquid to produce a second settled solids phase and a second aqueous phase;

(g) discharging said second aqueous phase to the environment or to reuse;

(h) transferring a portion of the second settled solids phase from the second treatment zone to the first treatment zone, thereby maintaining the desired concentration of aerobic biosolids and powdered adsorbent within the second treatment zone;

(i) adding sufficient powdered adsorbent to said second treatment zone to compensate for powdered adsorbent transferred to said first treatment zone in step (h); and

(j) removing a sufficient amount of anaerobic mixed liquor from said first treatment zone to control solids concentration therein.

2. A process according to claim 1 wherein said anaerobic first treatment zone comprises a lower digestion and mixing zone and an upper digestion and clarification zone, and said separating means of step (c) comprises a filter bed of support material within said upper digestion and clarification zone.

3. A process according to claim 1 wherein said anaerobic first treatment zone comprises a mixing digestion zone and a quiescent clarifier zone, and said separating means of step (c) comprises a baffle separating said mixing zone from said quiescent zone allowing liquid/solids separation within said quiescent zone.

4. A process according to claim 1 wherein said powdered adsorbent is powdered activated carbon.

5. A process according to claim 1 wherein a predetermined amount of first aqueous phase is transferred from said first treatment zone to said second treatment zone.

6. A process according to claim 5 wherein said second aerobic treatment zone comprises an aeration basin containing aeration and mixing means, said aerating and mixing step (e) occurring during and/or after the transfer of said predetermined amount of said first aqueous phase to the aeration basin, said separating step (f) and discharging step (g) occurring after completion of the aerating and mixing step (e).

7. A process according to claim 6 wherein said transferring step (h) of a portion of the second settled solids phase to the first treatment zone occurs during said separating step (f) or discharging step (g) within said aeration basin.

8. A process according to claim 6 wherein said powdered adsorbent adding step (i) occurs during said aerating and mixing step (e) in said aeration basin.

9. A process according to claim 6 wherein said mixing step (e) is assisted by mechanical mixing means within said aeration basin.

10. A process according to claim 1 wherein said first aqueous phase is continuously transferred from said first treatment zone to said second treatment zone.

11. A process according to claim 10 wherein said second aerobic treatment zone comprises a plurality of aeration basins, each basin containing an aeration means;

in step (d) said first aqueous phase flows from said first treatment zone to one of said basins for a predetermined fill period then to a different one of said basins for a predetermined fill period and this sequence is continued;

in step (e) said aerating and mixing is carried out in each of said basins during and/or after said filling period therefor;

in step (f) said separating is carried out in each basin after termination of said aerating and mixing period therefor;

in step (g) said discharging of said second aqueous phase from each of said basins occurs after completion of said separating step therefor and before commencement of the flow of said first aqueous phase from said first treatment zone thereinto.

12. A process according to claim 11 wherein step (d) is continued until the liquid level of said first aqueous phase in each of said basins reaches a predetermined upper level.

13. A process according to claim 11 wherein step (g) is continued until the liquid level of said second aqueous phase in each of said basins drops to a predetermined lower limit.

14. A process according to claim 11 wherein transferring step (h) of said second solids phase to said first treatment zone occurs during said separating step (f) or said discharging step (g) within each of said basins.

15. A process according to claim 11 wherein powdered adsorbent adding step (i) occurs during said transferring step (d) or aerating and mixing step (e) within each of said basins.

16. A process according to claim 11 wherein said mixing and aerating step (e) is assisted by mechanical mixing means within each of said basins.

17. A process according to claim 10 wherein said second treatment zone comprises an aeration basin including an inlet section and an aerating and mixing section substantially isolated from and in continuous fluid communication with said inlet section;

in transferring step (d) said first aqueous phase continuously flows from said first treatment zone into said inlet section at a first flow rate and passes therefrom into said aerating and mixing section;

in steps (e) and (f) said aerating and mixing and said separating steps are carried out in said aerating and mixing section; and

said separating step (f) and discharging step (g) occurring after completion of the aerating and mixing step (e); and

in step (g) said second aqueous phase is discharged from said aerating and mixing section at a second flow rate greater than said first flow rate until the liquid level of said second aqueous phase in said basin drops to a predetermined lower limit.

18. A process according to claim 17 wherein transferring step (h) of said second solids phase to said first treatment zone occurs during said separating step (f) or said discharging step (g) within said aeration basin.

19. A process according to claim 17 wherein powdered adsorbent adding step (i) occurs during said aerating and mixing step (e) within said aeration basin.

20. A process according to claim 19 wherein said powdered adsorbent is added to said inlet section of said aeration basin.

21. A process according to claim 17 wherein said mixing and aerating step (e) is assisted by mechanical mixing means within said aeration basin.

22. A process according to claim 10, wherein said second treatment zone comprises an aeration basin containing an aeration and mixing means followed by a settler/clarifier basin;

in step (d) said first aqueous phase continuously flows from said first treatment zone into said aeration basin;

in step (e) said aeration and mixing occurs continuously within said aeration basin;

in step (f) said aerobic mixed liquor continuously flows from said aeration basin to said settler/clarifier basin wherein said separating occurs,

in step (g) said second aqueous phase is discharged from said settler/clarifier basin; and

in step (h) a second portion of said second settled solids phase from said settler/clarifier basin is recycled to said aeration basin in addition to said portion which is transferred to said first treatment zone.

23. A process according to claim 22 wherein said powdered adsorbent is added to said aeration basin.

24. A process according to claim 22 wherein said aerating and mixing step (e) is assisted by mechanical mixing means within said aeration basin.

25. A process according to claim 1 wherein said first anaerobic treatment zone contains 500 to 30,000 mg/l of biosolids and 500 to 30,000 mg/l of powdered adsorbent.

26. A process according to claim 1 wherein said second aerobic treatment zone contains 10 to 50,000 mg/l of biosolids and 50 to 20,000 mg/l of powdered adsorbent.

27. A two-stage process for treating wastewater containing a COD of 5,000-50,000 mg/l comprising the steps;

(a) contacting said wastewater with anaerobic biosolids and powdered activated carbon in an anaerobic first treatment zone to form an anaerobic mixed liquor and remove a substantial portion of the COD from said wastewater;

(b) separating a fuel gas from said anaerobic mixed liquor within said first treatment zone;

(c) separating a substantial portion of the anaerobic biosolids and powdered activated carbon from said anaerobic mixed liquor by separating means within said first treatment zone to produce a first solids phase and a first aqueous phase;

(d) transferring continuously said first aqueous phase from said first treatment zone to an aeration basin;

(e) aerating and mixing continuously said first aqueous phase with an oxygen-containing gas in said aeration basin containing aerobic mixed liquor solids composed of aerobic biosolids and powdered activated carbon, to remove a substantial portion of the remaining COD from said first aqueous phase;

(f) transferring continuously said aerobic mixed liquor solids and thus-treated first aqueous phase to a settler/clarifier basin;

(g) settling said mixture of solids and liquid to form a settled second solids phase and a clarified second aqueous phase;

(h) discharging said second aqueous phase to the environment or to reuse;

(i) recycling at least a portion of said second settled solids phase from said clarifier to said aeration basin to maintain a desired concentration of biosolids and powdered activated carbon therein;

(j) transferring a portion of said second settled solids phase from said clarifier to said first anaerobic treatment zone thereby maintaining the desired concentration of biosolids and powdered activated carbon in said aeration basin;

(k) adding sufficient powdered activated carbon to said aeration basin to compensate for powdered activated carbon transferred to said first treatment zone in step (j); and

(l) removing a sufficient amount of anaerobic mixed liquor from said first treatment zone to control solids concentration therein.