Separating liquid suspensions

• US 5,624,580 A
• Filed: 02/28/1995
• Issued: 04/29/1997
• Est. Priority Date: 07/01/1993
• Status: Expired due to Term

• Current Assignee: Southern Water Services Limited (Greensand Holdings Ltd.)
• Original Assignee: Southern Water Services Limited (Greensand Holdings Ltd.)
• Inventors: De Hoxar, David
• Primary Examiner(s): Reifsnyder, David A.
• Application Number:
  US08/392,929
• Time in Patent Office: 791 Days
• Field of Search: 210/787, 210/788, 210/512.1, 210/512.3, 210/513, 210/521, 210/767, 210/800
• US Class Current: 210/800
• CPC Class Codes: B01D 21/0006 Settling tanks provided with means for cleaning and maintenance
• 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 21/0045 Plurality of essentially parallel plates
• CPC Class Codes: B01D 21/0087 Settling tanks provided with means for ensuring a special flow pattern, e.g. even inflow or outflow B01D21/2411 takes precedence
• CPC Class Codes: B01D 21/02 Settling tanks with single outlets for the separated liquid
• CPC Class Codes: B01D 21/2405 Feed mechanisms for settling tanks
• CPC Class Codes: B01D 21/2427 The feed or discharge opening located at a distant position from the side walls
• CPC Class Codes: B01D 21/2444 Discharge mechanisms for the classified liquid
• CPC Class Codes: B01D 21/245 Discharge mechanisms for the sediments
• CPC Class Codes: B01D 21/26 Separation of sediment aided by centrifugal force or centripetal forcecentrifuges B04B; cyclones B04C
• CPC Class Codes: B01D 21/30 Control equipment

Abstract

A method and apparatus for separating suspended solid particles and/or fluid droplets from a body of liquid is described. Fluid is caused to flow through at least one helical flow path defined between axially facing surfaces of a number of conical helical plates. Preferably, a substantially vertical flow channel of circular cross-section has disposed therein at least one conical helical plate with a diameter substantially equal to that of the flow channel. The conical helical plate or plates are arranged coaxially in the flow channel and define at least one helical flow path coaxial with the flow channel between axially facing surfaces of the plate or plates. The plate or plates are preferably capable of rotating about the axis of the flow channel, and may be driven. While they may be driven at a greater or lesser speed, they are preferably driven at a speed so as to approximately correspond with the flow rate of the liquid.

Claims

1. A method for separating a suspended phase from a body of liquid in a non-cyclonic gravity sedimentation separator, comprising introducing untreated liquid through an inlet into a flow channel in the sedimentation separator, coalescing the suspended phase to form a coalesced suspended phase and a treated liquid;

removing said treated liquid from the flow channel through a first outlet, and removing the coalesced suspended phase through a second outlet, arranging the location of the first outlet and the second outlet at locations spaced in vertical direction, configuring and orienting the inlet and the first and second outlets so as to impart substantially no circumferential motion to flow of liquid in the flow channel, and controlling the flow from the inlet to the first outlet so that it is in a vertical direction in the channel and is at a predetermined speed and wherein the liquid is constrained to flow at a predetermined rate through a vertical flow channel of circular cross-section wherein is situated at least one conical helical plate with a diameter substantially equal to that of the flow channel, the conical helical plate or plates being arranged coaxially in the flow channel and defining at least one helical flow path coaxial with the flow channel between facing surfaces of the plate or plates.

2. A method according to claim 1, further including the step of rotating the conical helical plate.

3. A method according to claim 2, wherein the helical plates have a speed of rotation and a pitch and they are arranged so that axial flow velocity of the liquid is from 60% to 140% of the product of the pitch and the speed of rotation.

4. A method of separating solid or liquid particles from a liquid according to claim 3, wherein axial flow velocity of the liquid is from 100% to 120% of the product of the pitch and the speed of rotation.

5. A method according to claim 1, wherein the liquid is caused to flow through a helical flow path by rotating the helical plate or plates in a body of liquid to be treated.