IP Library Granted Patent US 6,966,993
Granted Patent B2
US 6,966,993 · App. 10/470,934 · Granted Nov 22, 2005

Method and plant for thickening sludge derived from water treatment by flocculation-decantation with ballasted floc

Assignee: OTV S.A.
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Quick Facts
Patent No.
US 6,966,993
App. No.
10/470,934
Granted
Nov 22, 2005
Kind
B2
Abstract

A method is provided for thickening sludge produced through a ballasted flocculation process. The sludge and granular material from the ballasted flocculation process are directed to a sludge separator where the sludge is separated from the granular material. Thereafter the separated sludge is sent to a degassing area and the sludge is degassed. A flocculating agent is mixed or injected into the sludge. The sludge is directed to a sludge thickener with a load at a sill calculated on the surface of the thickener greater than 200 kgMIS/m 2 /day. This process produces a thickened sludge having a concentration greater than 10 gm/I.

Claims (18)

1. A method for thickening sludge produced by a ballasted flocculation water or wastewater treatment system comprising:

a. directing a mixture of sludge and granular material from the ballasted flocculation water or wastewater treatment system to a sludge separator and separating the sludge from the granular material;

b. directing the separated sludge to a degassing area and degassing the sludge;

c. injecting a flocculation agent into the sludge; and

d. directing the sludge to a sludge thickener with a load at a sill calculated on the sill surface of the thickener greater than 200 kgMIS/m 2 /day, and producing a thickened sludge having a concentration greater than 10 gm/l.

2. The method of claim 1 wherein the degassing of the sludge is implemented over a degassing surface corresponding to a superficial degassing speed of less than 100 m/hr.

3. The method of claim 1 including injecting at least one coagulating agent into the sludge.

4. The method of claim 3 wherein the injection of the coagulating agent occurs upstream from the injection of the flocculating agent.

5. The method of claim 1 wherein the degassing of the sludge is implemented over a degassing surface corresponding to a superficial degassing speed lower than 60 m/hr.

6. The method of claim 1 wherein the flocculating agent is mixed with the sludge in an agitated flocculation zone.

7. The method of claim 6 wherein the residency time of the sludge within the agitated flocculation zone is 10 minutes or less.

8. The method of claim 1 wherein the sludge thickening is carried out in a lamellar thickener.

9. The method of claim 8 wherein a sludge blanket is formed in the sludge thickener and the sludge thickener includes a series of plates that are spaced approximately 2 to 4 meters above a bottom portion of the thickener, and wherein the height of the sludge blanket is monitored and maintained between two predetermined heights.

10. The method of claim 1 wherein the sludge is produced from tertiary sewage treatment and the thickening process is carried out with a load at the sill greater than 300 kgMIS/m 2 /day and produces a concentration of thickened sludge greater than 15 gm/l.

11. The method of claim 1 wherein the sludge is produced from a primary sewage treatment or from combined sewage overflows resulting from rain, and wherein the thickening process is carried out with a load at the sill greater than 1000 kgMIS/m 2 /day and produces a thickened sludge having a concentration greater than 25 gm/l.

12. The method of claim 1 wherein the sludge to be thickened is produced from the settling treatment of surface waters other than carbonate removal treatment, and wherein the thickening process is carried out with a load at the sill greater than 200 kgMIS/m 2 /day and produces a sludge concentration of more than 10 gm/l.

13. The method of claim 1 including separating water from the thickened sludge and returning the separated water to the water or wastewater treatment system that produced the sludge.

14. The method of claim 1 wherein the flocculating agent is injected into the sludge in an area, and returning at least a portion of the thickened sludge from the sludge thickener to the area where the flocculating agent is injected into the sludge.

Assignments (2)
CHANGE OF NAME Recorded Jan 5, 2012
From: OTV S.A.
To: VEOLIA WATER SOLUTIONS & TECHNOLOGIES SUPPORT
Reel/Frame 027486/0098 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 1, 2003
From: BINOT, PATRICK
To: OTV S.A.
Reel/Frame 014721/0115 →
Priority Claims (1)
FR 01 01832 · Feb 9, 2001 · national
Continuity (1)
Related Publication 20040055961A1 · Mar 25, 2004