Method and installation for treating liquid by sedimentation using fine sand

• US 4,927,543 A
• Filed: 02/14/1989
• Issued: 05/22/1990
• Est. Priority Date: 02/25/1988
• Status: Expired due to Term

• Current Assignee: OTV S.A.
• Original Assignee: Omnium Detraitements et Devalorisation
• Inventors: Bablon, Guy P., Desbos, Gilbert
• Primary Examiner(s): Jones, W. Gary
• Assistant Examiner(s): Upton, Christopher
• Application Number:
  US07/310,204
• Time in Patent Office: 462 Days
• Field of Search: 210/711, 210/738, 210/768, 210/802, 210/803, 210/205, 210/207, 210/208, 210/519, 210/521, 210/522, 210/534
• US Class Current: 210/711
• CPC Class Codes: B01D 21/0018 provided with a pump mounted in or on a settling tank
• CPC Class Codes: B01D 21/0039 Settling tanks provided with contact surfaces, e.g. baffles, particles
• CPC Class Codes: B01D 21/0042 Baffles or guide plates
• CPC Class Codes: B01D 21/0045 Plurality of essentially parallel plates
• CPC Class Codes: B01D 21/0057 with counter-current flow direction of liquid and solid particles
• CPC Class Codes: B01D 21/01 using flocculating agents for purifying water C02F1/52; for liquid radioactive waste G21F9/10
• CPC Class Codes: B01D 21/02 Settling tanks with single outlets for the separated liquid
• CPC Class Codes: B01D 21/2427 The feed or discharge opening located at a distant position from the side walls
• CPC Class Codes: B01D 21/2472 Means for fluidising the sediments, e.g. by jets or mechanical agitators
• CPC Class Codes: B01D 21/2488 bringing about a partial recirculation of the liquid, e.g. for introducing chemical aids
• CPC Class Codes: C02F 2305/12 Inert solids used as ballast for improving sedimentation C02F3/1226 takes precedence

Abstract

Method of treating liquid by sedimentation in which reagents are injected into a flow of untreated liquid and there is created in the flow a colloid mixing and stabilization area; the flow is passed into an intermediate aggregation area and then into a sedimentation area equipped with separator plates from which clarified liquid is taken; characterized in that insoluble granular material which is more dense than the liquid is injected into the liquid in predetermined proportions in the mixing area where the flow is made turbulent, turbulence is induced in the intermediate aggregation area to maintain the granular material in suspension, virtually all of the granular material is brought into the sedimentation area, the sludge recovered in the sedimentation area is removed, the granular material is removed therefrom (D) and is recycled after cleaning.

Claims

1. A method for liquid treatment by sedimentation comprising the steps of:

injecting reagents into a flow of untreated liquid and creating in said flow a colloid mixing and destabilization area where said flow is made turbulent and where insoluble granular material denser than said liquid is injected into said liquid in predetermined proportions;

passing said liquid flow with said insoluble granular material into an intermediate colloid aggregation area where turbulence is induced to maintain said insoluble granular material in suspension,

passing said turbulent liquid flow together with subsequentially all of said granular material into a sedimentation area equipped with separator plates and removing clarified liquid from said separator plates; and

removing from the sedimentation area sludge formed therein including said insoluble granular material, recovering said insoluble granular material from said sludge, and cleaning and recycling said granular material.

2. Method according to claim 1 wherein there is maintained in the mixing area a speed gradient significantly greater than that maintained in the intermediate aggregation area.

3. Method according to claim 1 wherein said granular material is fine sand and there is established in the intermediate aggregation area a speed gradient between 400 and 1,500 s^-1.

4. Method according to claim 1 wherein said granular material is fine sand and there is established in the mixing area a speed gradient between 1,500 and 4,000 s^-1.

5. Method according to claim 1 wherein said granular material is fine sand and there are established a speed gradient in the mixing area between 3000 and 35000 s^-1 and a speed gradient in the aggregation area between 700 and 900 s^-1.

6. Method according to claim 1 wherein said granular material is fine sand with a particle size between 20 and 200 μ

m and said sand is injected with a concentration relative to the untreated liquid between approximately 1 and 4 g/l.

7. Method according to claim 1 wherein the time for which the liquid is in the intermediate aggregation area is between 2.5 and 3.5 times the time the liquid is in the mixing area.

8. Method according to claim 1 wherein said liquid flows upwardly in the mixing area and downwardly in the intermediate aggregation area.

10. A method according to claim 1 wherein said granular material is active chemically or biologically.

9. A method according to 1 wherein said granular material is substantially inert chemically biologically.

11. Installation for liquid treatment by sedimentation comprising:

a colloid mixing and destabilizing chamber provided with an inlet for untreated liquid, a reagent inlet, an inlet for introducing granular material insoluble in and denser than said liquid, a first turbulent flow inducing agitator device means, and a liquid outlet;

an intermediate aggregation chamber connected to said outlet of said colloid mixing and destabilizing chamber and provided with a second turbulent flow inducing agitation device means for maintaining said granular material in suspension and a liquid outlet;

a sedimentation chamber connected to said outlet out said intermediate aggregation chamber for receiving turbulent flow therefrom, said sedimentation chamber including separator plates and provided in an upper part thereof with an outlet for clarified liquid located above said separator plates and in a lower part with a sludge recovering area below the separator plates having an outlet for sludge; and

a sludge/granular material separator station connected to said outlet for sludge and to said inlet for granular material.

12. Installation according to claim 11 wherein said mixing chamber and said intermediate aggregation chamber are approximately square in cross-section and the ratio between the dimension of each chamber and the diameter of the corresponding agitator device is between approximately 0.5 and 0.8.

13. Installation according to claim 11 wherein said agitator device in said mixing chamber is a paddlewheel rotated about a vertical axis by motor means for imparting to the paddle blades peripheral speeds between 1 and 2 m/s and said agitator device of said intermediate aggregation chamber is a paddlewheel rotated about a vertical axis by motor means for imparting to the paddle blades peripheral speeds between 0.2 and 2.5 m/s.

14. Installation according to claim 11 wherein circulation of the liquid from said mixing chamber is achieved by overflow over a horizontal upper edge of a first separator wall between said mixing chamber and said intermediate aggregation chamber, by underflow beneath a horizontal edge of a second separator wall between said intermediate aggregation chamber and a lateral chamber, by overflow over an upper edge of a separator partition between said lateral chamber and a lateral distribution passage running along the length of said sedimentation chamber, and then by underflow under a lower edge of a separator wall between said lateral distribution passage and said sedimentation chamber. Said lower edge being inclined upwardly in the direction away from said lateral chamber.

15. Installation according to claim 14 wherein said intermediate aggregation chamber is approximately square in cross-section, vertical distance between said upper edge of said first wall and said lower edge of said second wall is between 1 and 3 times the side dimension of said intermediate aggregation chamber and said agitator device is situated relative to said upper edge of said wall at a depth between 0.5 and 0.9 times this vertical distance.

16. Installation according to claim 14 wherein said inclined lower edge of said separation wall between said lateral distribution passage and said sedimentation chamber rises from approximately the level of the lower edge of said separation wall between said intermediate aggregation chamber and said lateral chamber.

17. Installation according to claim 14 wherein the bottom of the sedimentation chamber is provided with means adapted to circulate the sludge towards a concentration area situated approximately underneath said intermediate aggregation chamber with which it communicates and connected to a sludge offtake channel.

18. Installation according to claim 17 wherein the bottom of the sedimentation chamber is inclined towards said concentration area.

19. Installation according to 11 wherein said agitator device of said intermediate aggregation chamber is an axial flow screw.

20. Installation according to claim 19 further comprising means for driving said axial flow screw in a direction tending to oppose the flow of the liquid;

and wherein said installation comprises means for directed said liquid flow upwardly in the mixing chamber and means for directing the liquid flow downwardly in the intermediate aggregation chamber.