Water treatment method by ballasted floc including a recycling of granular material

• US 6,645,386 B1
• Filed: 06/18/2001
• Issued: 11/11/2003
• Est. Priority Date: 11/18/1998
• Status: Expired due to Term

• Current Assignee: OTV SA SA
• Original Assignee: OTV SA SA
• Inventors: Binot, Patrick, Moreau, Pascal, Boissonnade, Genevieve
• Primary Examiner(s): Hruskoci, Peter A.
• Application Number:
  US09/807,850
• Time in Patent Office: 876 Days
• Field of Search: 210/711, 210/713, 210/714, 210/721, 210/724, 210/725, 210/727, 210/728, 210/738, 210/758, 210/759, 210/760, 210/754, 210/772, 210/787, 210/788, 210/764
• US Class Current: 210/711
• CPC Class Codes: B01D 21/01 using flocculating agents for purifying water C02F1/52; for liquid radioactive waste G21F9/10
• CPC Class Codes: B01D 21/26 Separation of sediment aided by centrifugal force or centripetal forcecentrifuges B04B; cyclones B04C
• CPC Class Codes: B01D 21/267 by using a cyclone
• CPC Class Codes: B03B 5/34 Applications of hydrocyclones
• CPC Class Codes: B04C 5/18 with auxiliary fluid assisting discharge
• CPC Class Codes: C02F 1/5281 Installations for water purification using chemical agents

Abstract

The invention concerns a flocculation-decantation method by ballasted flocs using a granular material and a step which consists in treating the sludge derived from flocculation-decantation in a circular grit trap wherein the auxiliary liquids tangentially injected into the sludge substantially in the same direction as the latter. The invention also concerns a circular grit trap with a cylindrical part of diameter D tangentially supplied with the suspension to be treated and a conical part and provided with a cylindrical chamber injecting wash-water provided at the conical part outlet and having a diameter D′ ranging between 0.35 D and 0.65 D, said cylindrical chamber having at least a tangential supply of auxiliary liquid along the same feeding direction as said tangential supply of the suspension to be treated.

Claims

1. A method of treating water or wastewater comprising:

a. treating the water or wastewater in a treatment facility by a ballasted flocculation process which produces sludge containing granular material;

b. directing the sludge into a circular grit trap having a cylindrical section, a conical section, and an upflow outlet, and separating substantial sludge from the granular material as the sludge moves around the cylindrical and conical sections of the circular grit trap, and wherein the separated sludge is discharged through the upflow outlet;

c. directing the remaining sludge and granular material from the conical section into a washing chamber;

d. injecting an auxiliary liquid into the chamber and washing the granular material to further separate sludge from the granular material;

e. directing the sludge separated from the granular material in the chamber back up through the grit trap and out the upflow outlet; and

f. directing the separated granular material from the chamber and recycling the separated granular material back to the treatment facility.

2. The method of claim 1 wherein the auxiliary liquid is injected into the chamber at a flow rate of between 50% and 200% of the flow rate out of the chamber less the flow rate of granular material passing from the chamber.

3. The method of claim 1 wherein injecting an auxiliary liquid into the chamber includes injecting water into the chamber.

4. The method of claim 3 wherein the auxiliary liquid further comprises at least one washing, disinfecting, or ballasted flocculation promoter agent.

5. The method of claim 4 wherein the agent is selected from the group consisting of sodium hydroxide, hydrochloric, sulphuric, nitric, phosphoric, citric, formic, carbonic acids, bleach, dissolved chlorine, chlorine dioxide, gaseous or dissolved ozone, hydrogen peroxide, aluminum or iron salts, and flocculation polymers.

6. The method of claim 1 wherein the chamber is generally cylindrical and has a diameter of approximately 35% to 65% of the diameter of the cylindrical section of the circular grit trap.

7. The method of claim 1 wherein the conical section of the circular grit trap forms an angle of approximately 30°

to 150°

.

8. The method of claim 1 wherein the conical section of the circular grit trap forms an angle of approximately 55°

to 80°

.

9. A method of recovering granular material used in a wastewater or water treatment process that produces a mixture of sludge and granular material, comprising:

a. directing the sludge and granular material mixture into a circular grit trap that includes an upflow outlet and a downflow outlet;

b. separating substantial sludge from the granular material as the mixture of sludge and granular material moves through the grit trap with the separated sludge moving through the upflow outlet and out of the grit trap;

c. directing the residual sludge and the granular material through the downflow outlet and into a washing chamber;

d. injecting an auxiliary liquid into the washing chamber and washing the granular material and further separating the residual sludge from the granular material such that separated residual sludge flows back into the circular grit trap and is discharged therefrom via the upflow outlet; and

e. directing the separated granular material from the washing chamber and recycling the separated granular material back to a wastewater or water treatment facility.