Multiple zone batch treatment process

• US 5,192,442 A
• Filed: 12/02/1991
• Issued: 03/09/1993
• Est. Priority Date: 12/02/1991
• Status: Expired due to Term

• Current Assignee: Siemen Water Technologies Corporation (Siemens AG)
• Original Assignee: Zimpro Passavant Environment Systems Incorporated
• Inventors: Piccirillo, John, Meidl, John A.
• Primary Examiner(s): Silverman, Stanley S.
• Assistant Examiner(s): Upton, Christopher
• Application Number:
  US07/801,211
• Time in Patent Office: 463 Days
• Field of Search: 210/605, 210/616, 210/620, 210/622, 210/623, 210/624, 210/626, 210/630, 210/744, 210/903, 210/220, 210/221.2
• 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 3/10 Packings; Fillings; Grids packing elements in general B01J19/30, B01J19/32
• CPC Class Codes: C02F 3/121 Multistep treatment
• 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 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/903 Nitrogenous

Abstract

A process is described for the operation of a multiple zone batch treatment system for biological or biophysical treatment of wastewater. The system comprises two or more batch treatment zones with wastewater passing sequentially through all treatment zones. After the mix and settle batch steps occur for all zones, influent wastewater flows into the first zone and displaces clarified wastewater in a plug flow mode through each treatment zone and ultimately from the last zone. The combining of the decant and fill steps for all or most of the zones provides for shorter cycle times and greater capacity for the system.

Claims

1. A process for operating a multiple zone batch treatment system for wastewater, said system comprising at least a first batch treatment zone and a last batch treatment zone, influent wastewater treated by sequential passage into and from said first zone, through any intervening zones, into and from said last zone, each treatment zone fitted with means to produce plug flow of liquid through that zone, the process comprising the steps;

a) mixing a biomass solids mixture with wastewater within each treatment zone;

b) settling each zone by ceasing mixing to produce a settled solids phase and a clarified liquid phase within each treatment zone;

c) transferring wastewater between adjacent zones in said system by adding a predetermined volume of influent liquid in a plug flow mode to at least one of said treatment zones, said added volume of influent liquid displacing a like volume of clarified liquid phase in a plug flow mode from that treatment zone to a following treatment zone; and

d) repeating steps a through c.

2. A process for operating a multiple zone batch treatment system for wastewater, said system comprising at least a first batch treatment zone and a last batch treatment zone, influent wastewater treated by sequential passage into and from said first zone, through any intervening zones, into and from said last zone, each treatment zone fitted with an inlet means to produce plug flow of liquid into and out of that zone, the process comprising the steps;

a) mixing a biomass solids mixture with wastewater within each treatment zone;

b) settling each zone by ceasing mixing to produce a settled solids phase and a clarified liquid phase within each treatment zone;

c) adding a first predetermined volume of influent wastewater to said first batch treatment zone through said inlet means therein to displace clarified liquid phase in a plug flow mode from said first zone, through any intervening treatment zones in a plug flow mode via said inlet means therein, thereby displacing a second predetermined volume of clarified liquid phase effluent, essentially equal to said added first predetermined volume, from said last batch treatment zone; and

d) repeating steps a through c.

3. A process according to claim 2 wherein said inlet means is a pipe manifold with multiple outlets.

4. A process according to claim 2 wherein said inlet means is a baffle with a plurality of apertures therein.

5. A process according to claim 2 wherein said mixing step is accomplished by aerating means.

6. A process according to claim 2 wherein said mixing step is accomplished by mechanical means.

7. A process according to claim 2 further comprising operating said treatment system with biomass solids plus powdered adsorbent in each treatment zone to effect biophysical treatment of wastewater.

8. A process according to claim 7 wherein said powdered adsorbent is added only to said last treatment zone and settled biomass solids plus powdered adsorbent are transferred from said last zone, through any intervening zones, to said first zone, countercurrent to said influent wastewater flow.

9. A process according to claim 8 wherein said biomass solids plus powdered adsorbent are wasted from said first batch treatment zone to control solids concentration within said treatment system.

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

11. A process for operating a multiple zone batch treatment system for wastewater, said system comprising at least a first batch treatment zone and a last batch treatment zone, influent wastewater treated by sequential passage into and from said first zone, through any intervening zones, into and from said last zone, each treatment zone except said last zone fitted with an inlet means to produce plug flow of liquid into and out of that zone, the process comprising the steps;

a) mixing a biomass solids mixture with wastewater within each treatment zone;

b) settling each zone by ceasing mixing to produce a settled solids phase and a clarified liquid phase within each treatment zone;

c) removing a first predetermined volume of clarified liquid phase effluent from said last batch treatment zone;

d) adding a second predetermined volume of influent wastewater, essentially equal to said removed first predetermined volume, to said first batch treatment zone through said inlet means therein to displace clarified liquid phase in a plug flow mode from said first zone, through any intervening treatment zones in a plug flow mode via said inlet means therein, to said last treatment zone; and

e) repeating steps a through d.

12. A process according to claim 11 wherein said inlet means is a pipe manifold with multiple outlets.

13. A process according to claim 11 wherein said inlet means is a baffle with a plurality of apertures therein.

14. A process according to claim 11 wherein said mixing step is accomplished by aerating means.

15. A process according to claim 11 wherein said mixing step is accomplished by mechanical means.

16. A process according to claim 11 wherein said predetermined volume of influent added to said first treatment zone is determined by a controller with a level sensor located in said last treatment zone, said level sensor set to control the wastewater at a specific maximum level within all treatment zones of the system.

17. A process according to claim 11 further comprising operating said treatment system with biomass solids plus powdered adsorbent in each treatment zone to effect biophysical treatment of wastewater.

18. A process according to claim 17 wherein said powdered adsorbent is added only to said last treatment zone and settled biomass solids plus powdered adsorbent are transferred from said last zone, through any intervening zones, to said first zone, countercurrent to said influent wastewater flow.

19. A process according to claim 18 wherein said biomass solids plus powdered adsorbent are wasted from said first batch treatment zone to control solids concentration within said treatment system.

20. A process according to claim 17 wherein said powdered adsorbent is powdered activated carbon.

21. A process for operating a multiple zone batch treatment system for wastewater, said system comprising at least a first batch treatment zone and a last batch treatment zone, influent wastewater treated by sequential passage into and from said first zone, through any intervening zones, into and from said last zone, each treatment zone fitted with an inlet means to produce plug flow of liquid into and out of that zone, the process comprising the steps;

a) mixing a biomass solids mixture with wastewater within each treatment zone;

b) settling each zone by ceasing mixing to produce a settled solids phase and a clarified liquid phase within each treatment zone;

c) removing a first predetermined volume of clarified liquid phase effluent from said last batch treatment zone while simultaneously adding a second predetermined volume of influent wastewater, essentially equal to said added first predetermined volume, to said first batch treatment zone through said inlet means therein to displace clarified liquid phase in a plug flow mode from said first zone, through any intervening treatment zones in a plug flow mode via said inlet means therein, to said last batch treatment zone; and

d) repeating steps a through c.

22. A process for operating a multiple zone batch treatment system for wastewater, said system comprising a first aerobic carbonaceous removal zone, a second aerobic nitrification zone, a third anoxic/anaerobic denitrification zone and a fourth aerobic adsorbent treatment zone;

influent wastewater treated by sequential passage into and from said first zone, through said second and third zones, into said fourth zone and then exiting said treatment system;

said zones each fitted with an inlet means to produce plug flow of liquid into and out of each of said zones, the process comprising the steps;

(a) mixing and aerating a biomass solids and powdered adsorbent mixture with wastewater within said first, second and fourth treatment zones, and mechanically mixing said biomass solids and adsorbent mixture with wastewater within said third treatment zone;

(b) settling each zone by ceasing said mixing and aerating to produce a settled solids phase and a clarified liquid phase within each zone;

(c) adding a first predetermined volume of influent wastewater to said first batch treatment zone through said inlet means therein to displace clarified liquid phase in a plug flow mode from said first zone, through said second and third zones in a plug flow mode via said inlet means therein, thereby displacing a second predetermined volume of clarified liquid phase effluent, essentially equal to said added first predetermined volume, from said fourth batch treatment zone in a plug flow mode; and

(d) repeating steps (a) through (c).

23. A process according to claim 22 wherein said powdered adsorbent is added only to said last treatment zone and settled biomass solids plus powdered adsorbent are transferred from said last zone, through any intervening zones, to said first zone, countercurrent to said influent wastewater flow.

24. A process according to claim 23 wherein said biomass solids plus powdered adsorbent are wasted from said first batch treatment zone to control solids concentration within said treatment system.

25. A process according to claim 22 wherein said powdered adsorbent is powdered activated carbon.

26. A process according to claim 22 further comprising the step of recycling for nutrient removal a portion of said clarified liquid phase from a given treatment zone to an upstream treatment zone during said step (c) of adding influent wastewater to said first treatment zone.

27. A process for operating a multiple zone batch treatment system for wastewater, said system comprising a first aerobic carbonaceous removal zone, a second aerobic nitrification zone, a third anoxic/anaerobic denitrification zone and a fourth aerobic adsorbent treatment zone;

influent wastewater treated by sequential passage into and from said first zone, through said second and third zones, to said fourth zone and then exiting said treatment system;

said first, second and third zones each fitted with an inlet means to produce plug flow of liquid into and out of each of said three zones, the process comprising the steps;

(a) mixing and aerating a biomass solids and powdered adsorbent mixture with wastewater within said first, second and fourth treatment zones, and mechanically mixing said biomass solids and adsorbent mixture with wastewater within said third treatment zone;

(b) settling each zone by ceasing said mixing and aerating to produce a settled solids phase and a clarified liquid phase within each zone;

(c) removing a first predetermined volume of clarified liquid phase effluent from said fourth batch treatment zone;

(d) adding a second predetermined volume of influent wastewater, essentially equal to said removed first predetermined volume, to said first batch treatment zone through said inlet means therein to displace clarified liquid phase in a plug flow mode from said first zone, through said second and third zones in a plug flow mode via said inlet means therein, to said fourth treatment zone; and

(e) repeating steps (a) through (d).

28. A process according to claim 27 wherein said powdered adsorbent is added only to said last treatment zone and settled biomass solids plus powdered adsorbent are transferred from said last zone, through any intervening zones, to said first zone, countercurrent to said influent wastewater flow.

29. A process according to claim 28 wherein said biomass solids plus powdered adsorbent are wasted from said first batch treatment zone to control solids concentration within said treatment system.

30. A process according to claim 27 wherein said powdered adsorbent is powdered activated carbon.

31. A process according to claim 27 further comprising the step of recycling for nutrient removal a portion of said clarified liquid phase from a given treatment zone to an upstream treatment zone during said step (c) of adding influent wastewater to said first treatment zone.

32. A process for operating a multiple zone batch treatment system for wastewater, said system comprising a first anoxic/anaerobic carbonaceous removal zone, a second aerobic nitrification zone, a third anoxic/anaerobic denitrification zone and a fourth aerobic adsorbent treatment zone;

influent wastewater treated by sequential passage from said first zone, through said second and third zones, to said fourth zone and then exiting said treatment system;

said first, second and third zones each fitted with an inlet means to produce plug flow of liquid into and out of each of said three zones, the process comprising the steps;

(a) mixing and aerating a biomass solids and powdered adsorbent mixture with wastewater within said second and fourth treatment zones, and mechanically mixing said biomass solids and adsorbent mixture with wastewater within said first and third treatment zones;

(b) settling each zone by ceasing said mixing and aerating to produce a settled solids phase and a clarified liquid phase within each zone;

(c) removing a first predetermined volume of clarified liquid phase effluent from said fourth batch treatment zone;

(d) adding a second predetermined volume of influent wastewater, essentially equal to said removed first predetermined volume, to said first batch treatment zone through said inlet means therein to displace clarified liquid phase in a plug flow mode from said first zone, through said second and third zones in a plug flow mode via said inlet means therein, to said fourth treatment zone; and

(e) repeating steps (a) through (d).

33. A process according to claim 32 wherein said powdered adsorbent is added only to said last treatment zone and settled biomass solids plus powdered adsorbent are transferred from said last zone, through any intervening zones, to said first zone, countercurrent to said influent wastewater flow.

34. A process according to claim 33 wherein said biomass solids plus powdered adsorbent are wasted from said first batch treatment zone to control solids concentration within said treatment system.

35. A process according to claim 32 wherein said powdered adsorbent is powdered activated carbon.

36. A process according to claim 32 further comprising the step of recycling for nutrient removal a portion of said clarified liquid phase from a given treatment zone to an upstream treatment zone during said step (c) of adding influent wastewater to said first treatment zone.