Method of treating water with an inorganic powder reagent

• US 7,678,278 B2
• Filed: 09/29/2006
• Issued: 03/16/2010
• Est. Priority Date: 09/29/2006
• Status: Active Grant

• Current Assignee: Veolia Water Solutions & Technologies Support
• Original Assignee: OTV SA SA
• Inventors: Roche, Pascal, Binot, Patrick, Gaid, Abdelkader
• Primary Examiner(s): Savage; Matthew O
• Application Number:
  US11/536,771
• Publication Number:
  US 20080078721A1
• Time in Patent Office: 1,264 Days
• Field of Search: 210/661, 210/669, 210/694, 210/748, 210/663, 210/665, 210/666, 210/667, 210/754
• US Class Current: 210/661
• CPC Class Codes: C02F 1/28 by sorption using ion-exchange C02F1/42; sorbent compositions B01J
• CPC Class Codes: C02F 1/283 using coal, charred products, or inorganic mixtures containing them
• CPC Class Codes: C02F 1/32 with ultraviolet light
• CPC Class Codes: C02F 1/38 by centrifugal separation
• CPC Class Codes: C02F 1/44 by dialysis, osmosis or reverse osmosis general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration
• CPC Class Codes: C02F 1/52 by flocculation or precipitation of suspended impurities C02F1/463 takes precedence
• CPC Class Codes: C02F 1/5236 using inorganic agents
• CPC Class Codes: C02F 1/56 Macromolecular compounds
• CPC Class Codes: C02F 1/72 by oxidation C02F1/4672 takes precedence
• CPC Class Codes: C02F 2305/12 Inert solids used as ballast for improving sedimentation C02F3/1226 takes precedence
• CPC Class Codes: C02F 9/00 Multistage treatment of water, waste water or sewage

Abstract

A process for treating water is provided where the water is mixed with an inorganic reagent powder such as powder activated carbon. Organics and micropollutants are absorbed by the reagent powder. After the reagent powder has been mixed with the water, the water is directed to a setting tank and sludge from the water settles to produce a clarified effluent. Forming a part of the sludge is the reagent powder previously added. Sludge is collected and directed to a separator that separates the reagent powder from the sludge. Separated reagent powder is recycled and mixed with the water being treated.

Claims

1. A method of treating water using a dual ballasted flocculation system, comprising:

a. directing the water into a first ballasted flocculation system including a first treatment tank and a first clarifier disposed downstream from the first treatment tank;

b. directing the water into the first treatment tank and injecting a flocculent and ballast into the first treatment tank to form flocs;

c. directing the water containing flocs from the first treatment tank into the first clarifier, settling the flocs, and clarifying the water;

d. directing the flocs from the first clarifier to a first separator and separating the ballast from the flocs and recirculating at least a portion of the ballast into the first treatment tank;

e. after clarifying the water, directing the water from the first ballasted flocculation system to a second ballasted flocculation system including a second treatment tank and a second clarifier;

f. in the second treatment tank adding powdered activated carbon and ballast to the water and forming flocs containing powdered activated carbon;

g. directing the water and flocs containing powdered activated carbon from the second treatment tank into the second clarifier and settling the flocs containing powdered activated carbon;

h. directing the flocs containing powdered activated carbon from the second clarifier to a second separator and separating the powdered activated carbon from the flocs and recirculating a first portion of the powdered activated carbon into the second treatment tank.

2. The method of claim 1 wherein settling the flocs containing powdered activated carbon includes forming a clarified effluent and the method includes directing the clarified effluent to a membrane filter disposed downstream from the second ballasted flocculation system and filtering the clarified effluent.

3. The method of claim 1 including mixing a coagulant with the water in the first ballasted flocculation zone.

4. The method of claim 1 further comprising directing a second portion of the powdered activated carbon into the first treatment tank.

5. The method of claim 4 wherein the water directed to the first clarifier includes a turbidity higher than 2 NTU.

6. The method of claim 4 wherein the water is also treated by ultraviolet treatment.

7. The method of claim 1 wherein a powdered activated carbon concentration in the second treatment tank is maintained between approximately 5 kg/m³ and approximately 150 kg/m³.

8. The method of claim 1 further comprising separating the ballast from the flocs in the second separator and recirculating at least a portion of the ballast in the second treatment tank.

9. The method of claim 1 further comprising:

directing a second portion of the powdered activated carbon into the first treatment tank;

separating the ballast from the flocs in the second separator and recirculating at least a portion of the ballast in the second treatment tank; and

wherein a powdered activated carbon concentration in the second treatment tank is maintained between approximately 5 kg/m³ and approximately 150 kg/m³.

10. The method of claim 9 wherein settling the flocs containing powdered activated carbon includes forming a clarified effluent and the method includes directing the clarified effluent to a membrane filter disposed downstream from the second ballasted flocculation system and filtering the clarified effluent.

11. The method of claim 1 wherein after treating the water in the first and second ballasted flocculation systems the method further comprises treating the water with a disinfectant.

12. The method of claim 10 wherein the disinfectant is chlorine.