Treatment of highly colored wastewaters

• US 5,302,288 A
• Filed: 03/19/1993
• Issued: 04/12/1994
• Est. Priority Date: 03/19/1993
• Status: Expired due to Term

• Current Assignee: Siemens Energy Incorporated (Siemens AG)
• Original Assignee: Zimpro Environmental, Inc.
• Inventors: Meidl, John A., Vollstedt, Thomas J.
• Primary Examiner(s): Upton, Christopher
• Application Number:
  US08/035,110
• Time in Patent Office: 389 Days
• Field of Search: 210/603, 210/605, 210/616, 210/624, 210/626, 210/631, 210/668, 210/669, 210/756, 210/758, 210/759, 210/760, 210/691, 210/694
• US Class Current: 210/616
• CPC Class Codes: C02F 1/283 using coal, charred products, or inorganic mixtures containing them
• CPC Class Codes: C02F 1/72 by oxidation C02F1/4672 takes precedence
• CPC Class Codes: C02F 1/722 Oxidation by peroxides
• CPC Class Codes: C02F 1/76 with halogens or compounds of halogens C02F1/4674 takes precedence
• CPC Class Codes: C02F 3/02 Aerobic processes
• CPC Class Codes: C02F 3/1215 Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates
• CPC Class Codes: C02F 3/1226 comprising an absorbent material suspended in the mixed liquor
• CPC Class Codes: C02F 3/1263 Sequencing batch reactors [SBR]
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

The invention is a process for purifying wastewater containing organic and color-causing pollutants. The three unit processes include a first stage aerobic or anaerobic biophysical treatment, a second stage oxidizer treatment, and a third stage adsorbent contact treatment. The biophysical treatment removes the majority of the pollutants while the oxidizer treatment destroys residual organics and color-causing pollutants. The adsorbent contact treatment destroys any residual oxidizer in the wastewater and/or adsorbs any residual oxidation products. The preferred adsorbent is powdered activated carbon and the preferred oxidizer is some form of chlorine, e.g. sodium hypochlorite. The process may be operated in either a continuous flow mode or a batch flow mode.

Claims

1. A process for purifying wastewater containing organic and color-causing pollutants comprising the steps:

(a) providing a primary aerobic treatment zone including an aeration zone and a quiescent zone for treating the wastewater;

(b) introducing wastewater into said aeration zone;

(c) aerating the wastewater in said aeration zone with an oxygen-containing gas in the presence of sufficient amounts of powdered adsorbent solids and biologically active aerobic solids to reduce the organic and color-causing pollutants to desired levels, said thus-treated wastewater and solids transferred from said aeration zone to said quiescent zone;

(d) retaining said thus-treated wastewater and solids in the quiescent zone for a sufficient time for solids therein to settle by gravity and produce a first settled solids phase and a first aqueous phase substantially free of solids;

(e) transferring said first aqueous phase from said primary treatment zone to an oxidizer contact zone;

(f) contacting said first aqueous phase with a chemical oxidizer in the oxidizer contact zone for a sufficient time to remove a further portion of said organic and color-causing pollutants;

(g) transferring said thus-treated aqueous phase from the oxidizer contact zone to an adsorbent contact zone;

(h) agitating said thus-treated aqueous phase in the adsorbent contact zone in the presence of powdered adsorbent solids for an agitation period sufficient to further reduce the organic and color-causing pollutants to desired levels;

(i) terminating agitation and allowing adsorbent solids in said adsorbent-treated aqueous phase to settle by gravity for a settling period sufficient to produce a clarified, substantially solids-free, second aqueous phase and a second solids phase; and

(j) separating said second aqueous phase from said second solids phase and discharging said second aqueous phase to the environment or to further use.

2. A process according to claim 1 wherein said process operates in a continuous flow mode wherein

said aeration of wastewater of step (c) and said solids settling in quiescent zone of step (d) occurs continuously and simultaneously;

said oxidizing of wastewater of step (f) occurs continuously;

and said agitating of wastewater and adsorbent of step (h), settling of step (i), and separating of step (j) occurs continuously and simultaneously.

3. A process according to claim 1 wherein said process operates in a batch flow mode wherein

said aeration of wastewater of step (c) and said solids settling in quiescent zone of step (d) occur sequentially within the same space;

said oxidizing of wastewater of step (f) occurs intermittently; and

said agitating of wastewater and adsorbent of step (h), settling of step (i), and separating of step (j) occur sequentially within the same space.

4. A process according to claim 1 wherein the total amount of adsorbent solids and biologically active aerobic solids present in said aeration zone is about 50 to about 50,000 parts per million of wastewater.

5. A process according to claim 4 wherein the amount of adsorbent solids present in said aeration zone is about 25 to about 20,000 parts per million of wastewater.

6. A process according to claim 1 wherein the amount of adsorbent solids present in said adsorbent contact zone is about 50 to about 50,000 parts per million of wastewater.

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

8. A process according to claim 1 wherein said agitation in said adsorbent contact zone is carried out by introducing a pressurized oxygen-containing gas into said contact zone.

9. A process according to claim 1 wherein said agitation in said adsorbent contact zone is carried out by mechanical agitation in said contact zone.

10. A process according to claim 1 wherein said oxidizer is chosen from a group comprising Cl₂, NaOCl, KMnO₄, H₂ O₂, or O₃.

11. A process according to claim 10 wherein the amount of chlorine oxidizer used is about 50 to about 15,000 parts per million of wastewater.

12. A process according to claim 1 further comprising the step of adding to said thus-treated wastewater in step (c) a flocculation aid for promoting settling of solids in said quiescent zone of step (d).

13. A process according to claim 12 wherein said flocculation aid is a cationic polymer.

14. A process according to claim 1 further comprising the step of adding to said thus-treated aqueous phase in step (h) a flocculation aid for promoting settling of powdered adsorbent solids in said contact zone of step (i).

15. A process according to claim 14 wherein said flocculation aid is a cationic polymer.

16. A process according to claim 1 further comprising the step of transferring at least a portion of said second solids phase from said adsorbent contact zone to said primary aerobic treatment aeration zone.

17. A process according to claim 1 further comprising the step of withdrawing a portion of the powdered adsorbent solids and biologically active aerobic solids from said primary aerobic treatment zone so as to maintain the amounts of said adsorbent and biological solids present in said aeration zone at predetermined levels.

18. A process for purifying wastewater containing organic and color-causing pollutants comprising the steps:

(a) providing a primary anaerobic treatment zone including a mixing zone and a quiescent zone for treating the wastewater;

(b) introducing wastewater into said anaerobic mixing zone;

(c) mixing the wastewater in said mixing zone by mixing means in the presence of sufficient amounts of powdered adsorbent solids and biologically active anaerobic solids to reduce the organic and color-causing pollutants to desired levels, said thus-treated wastewater and solids transferred from said mixing zone to said anaerobic quiescent zone;

(d) retaining said thus-treated wastewater and solids in the quiescent zone for a sufficient time for solids therein to settle by gravity and produce a first settled solids phase and a first aqueous phase substantially free of solids;

(e) transferring said first aqueous phase from said primary anaerobic treatment zone to an oxidizer contact zone;

(f) contacting said first aqueous phase with a chemical oxidizer in the oxidizer contact zone for a sufficient time to remove a further portion of said organic and color-causing pollutants;

(g) transferring said thus-treated aqueous phase from the oxidizer contact zone to an adsorbent contact zone;

(h) agitating said thus-treated aqueous phase in the adsorbent contact zone in the presence of powdered adsorbent solids for an agitation period sufficient to further reduce the organic and color-causing pollutants to desired levels;

(i) terminating agitation and allowing adsorbent solids in said adsorbent-treated aqueous phase to settle by gravity for a settling period sufficient to produce a clarified, substantially solids-free, second aqueous phase and a second solids phase; and

(j) separating said second aqueous phase from said second solids phase and discharging said second aqueous phase to the environment or to further use.

19. A process according to claim 18 wherein said process operates in a continuous flow mode wherein

said mixing of wastewater of step (c) and said solids settling in quiescent zone of step (d) occurs continuously and simultaneously;

said oxidizing of wastewater of step (f) occurs continuously;

and said agitating of wastewater and adsorbent of step (h), settling of step (i), and separating of step (j) occurs continuously and simultaneously.

20. A process according to claim 18 wherein said process operates in a batch flow mode wherein

said mixing of wastewater of step (c) and said solids settling in quiescent zone of step (d) occur sequentially within the same space;

said oxidizing of wastewater of step (f) occurs intermittently; and

said agitating of wastewater and adsorbent of step (h), settling of step (i), and separating of step (j) occur sequentially within the same space.

21. A process according to claim 18 wherein the total amount of adsorbent solids and biologically active anaerobic solids present in said mixing zone is about 50 to about 50,000 parts per million of wastewater.

22. A process according to claim 21 wherein the amount of adsorbent solids present in said mixing zone is about 25 to about 20,000 parts per million of wastewater.

23. A process according to claim 18 wherein the amount of adsorbent solids present in said adsorbent contact zone is about 50 to about 50,000 parts per million of wastewater.

24. A process according to claim 18 wherein said adsorbent is activated carbon.

25. A process according to claim 18 wherein said agitation in said adsorbent contact zone is carried out by introducing a pressurized oxygen-containing gas into said contact zone.

26. A process according to claim 18 wherein said agitation in said adsorbent contact zone is carried out by mechanical agitation in said contact zone.

27. A process according to claim 18 wherein said oxidizer is chosen from a group comprising Cl₂,NaOCl, KMnO₄, H₂ O₂, or O₃.

28. A process according to claim 27 wherein the amount of chlorine oxidizer used is about 50 to about 15,000 parts per million of wastewater.

29. A process according to claim 18 further comprising the step of adding to said thus-treated wastewater in step (c) a flocculation aid for promoting settling of solids in said quiescent zone of step (d).

30. A process according to claim 29 wherein said flocculation aid is a cationic polymer.

31. A process according to claim 18 further comprising the step of adding to said thus-treated aqueous phase in step (h) a flocculation aid for promoting settling of powdered adsorbent solids in said contact zone of step (i).

32. A process according to claim 31 wherein said flocculation aid is a cationic polymer.

33. A process according to claim 18 further comprising the step of transferring at least a portion of said second solids phase from said adsorbent contact zone to said primary anaerobic treatment mixing zone.

34. A process according to claim 18 further comprising the step of withdrawing a portion of the powdered adsorbent solids and biologically active anaerobic solids from said primary anaerobic treatment zone so as to maintain the amounts of said adsorbent and biological solids present in said mixing zone at predetermined levels.