Method for the treatment of water by ballasted flocculation and gravity separation with variable function modes

• US 7,001,525 B2
• Filed: 03/14/2002
• Issued: 02/21/2006
• Est. Priority Date: 03/15/2001
• Status: Expired due to Fees

• Current Assignee: Veolia Water Solutions & Technologies Support
• Original Assignee: OTV SA SA
• Inventors: Ursel, Valery, Binot, Patrick
• Primary Examiner(s): Hruskoci, Peter A.
• Application Number:
  US10/471,848
• Publication Number:
  US 20040144730A1
• Time in Patent Office: 1,440 Days
• Field of Search: 210/709, 210/711, 210/713, 210/714, 210/724, 210/725, 210/727, 210/738, 210/787
• US Class Current: 210/709
• CPC Class Codes: B01D 21/0018 provided with a pump mounted in or on a settling tank
• CPC Class Codes: B01D 21/0024 Inlets or outlets provided with regulating devices, e.g. valves, flaps B01D21/24 takes precedence
• CPC Class Codes: B01D 21/003 Sedimentation tanks provided with a plurality of compartments separated by a partition wall B01D21/0039 takes precedence
• CPC Class Codes: B01D 21/0039 Settling tanks provided with contact surfaces, e.g. baffles, particles
• 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 21/0093 Mechanisms for taking out of action one or more units of a multi-unit settling mechanism
• CPC Class Codes: B01D 21/08 provided with flocculating compartments
• CPC Class Codes: B01D 21/2427 The feed or discharge opening located at a distant position from the side walls
• CPC Class Codes: B01D 21/2488 bringing about a partial recirculation of the liquid, e.g. for introducing chemical aids
• CPC Class Codes: B01D 21/267 by using a cyclone
• CPC Class Codes: B01D 21/30 Control equipment
• CPC Class Codes: B01D 21/32 Density control of clear liquid or sediment, e.g. optical control ; Control of physical properties
• CPC Class Codes: B01D 21/34 Controlling the feed distribution; Controlling the liquid level ; Control of process parameters
• CPC Class Codes: C02F 1/5281 Installations for water purification using chemical agents
• CPC Class Codes: C02F 2305/12 Inert solids used as ballast for improving sedimentation C02F3/1226 takes precedence

Abstract

The invention relates to a method for treatment of water, permitting the physico-chemical treatment of water, including a ballasted flocculation stage using a granular ballast material with a density greater than water, followed by, a stage of gravity separation of the treated water and the flocculent mass, a stage of separation of the granular material, recycled for the flocculation stage and the muds. Said muds are sent to a stage for treatment of the muds, characterised in comprising a stage in which the functional mode passes from a mode using ballasted flocculation and gravity separation using coagulation and flocculation reagents to a mode functioning by simple gravity separation, without using coagulation and flocculation reagents. The passage from one mode to another is determined using at least one item of information on the water obtained at any stage of the treatment thereof or before said treatment.

Claims

1. A method of treating water comprising at least three different operation modes including a first mode of treating the water with a ballasted flocculation process and including injecting into the water granular ballasting material denser than the water, a coagulant, and a flocculant to yield treated water, separating flocs from the treated water by a gravity separation step and separating granular material from the flocs leaving sludge that is directed to a sludge treatment process;

changing modes of operation by changing from the ballasted flocculation process to a second mode where contaminants in the water are separated by a gravity separation process without the use of coagulation and flocculation reagents; and

changing modes of operation from the second mode to a third mode wherein the water is treated with at least a chemical coagulation or flocculation reagent, but without granular ballasting material;

the changeover from one operating mode to another being determined based on at least one item of information related to the water at any step in the method of treatment and before the treatment.

2. Method according to claim 1, characterized in that the said granular ballasting material is micro-sand with an effective diameter of between 30 and 200 micrometers, and in which said gravity separation step is a settlement step.

3. Method according to claim 1, characterized in that the granular material is micro-sand with an effective diameter of between 30 and 200 micrometers, and the said gravity separation step is a centrifuging step.

4. Method according to claim 1, wherein at least one item of information about the water used to decide which operating mode should be used is chosen from among the water flow to be treated, turbidity of the water to be treated, turbidity of the treated water, Chemical Oxygen Demand (COD) of the water to be treated, Total Organic Carbon (T.O.C.), and resistivity.

5. Method according to claim 1, including using low speed stirrers to avoid bringing granular ballasting material back into suspension in the first mode wherein the speed is between 2.5 and 20 centimeters per second.

6. Method according to claim 5, wherein the speed of the stirrers used to avoid bringing granular ballasting material back into suspension in the first mode is between 5 and 10 centimeters per second.

7. Method according to claim 1, wherein the changeover changing from one operating mode to another is automatic.