US3542207A - Sedimentation tank with rotary sediment raking structure - Google Patents

Sedimentation tank with rotary sediment raking structure Download PDF

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Publication number
US3542207A
US3542207A US805568A US3542207DA US3542207A US 3542207 A US3542207 A US 3542207A US 805568 A US805568 A US 805568A US 3542207D A US3542207D A US 3542207DA US 3542207 A US3542207 A US 3542207A
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Prior art keywords
feedwell
annular
rake
main
arms
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Expired - Lifetime
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US805568A
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English (en)
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Keith C Stansmore
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Dorr Oliver Inc
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Dorr Oliver Inc
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Assigned to BANCBOSTON FINANCIAL COMPANY, A CORP OF CT reassignment BANCBOSTON FINANCIAL COMPANY, A CORP OF CT SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: DORR VENTURES, INC., A DE CORP.
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/02—Settling tanks with single outlets for the separated liquid
    • B01D21/04—Settling tanks with single outlets for the separated liquid with moving scrapers
    • B01D21/06—Settling tanks with single outlets for the separated liquid with moving scrapers with rotating scrapers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0003—Making of sedimentation devices, structural details thereof, e.g. prefabricated parts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/18—Construction of the scrapers or the driving mechanisms for settling tanks
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2405—Feed mechanisms for settling tanks
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2427—The feed or discharge opening located at a distant position from the side walls

Definitions

  • SEDIMENTATION TANK WITH ROTARY ABSTRACT A sedimentation tank Of the type wherein the SEDIMENT RAKING STRUCTURE rake arms of a rotary rake structure are linked to a cen tral ver- 11 Claims, 14 Drawing Figs. tical member such as a vertical shaft or cage, wrth mclined draft or drag elements connecting them to respective drive Us. Cl. u u arms paced upwardly from the rake arms and fixed to the yer- 210/528 tical member.
  • Improved feedwell means are structurally com- Illi- Clo u bined the drive arms comprising an auxiliary feedwell at [5 Field olSelrch 210/519, an upper
  • KEITH C STA/VSMORE UZ eM/rc ATTORNEY l alz ented Nov; 24, 1970 Sheet g of 5 INVENTOR.
  • KEITH C STA/VSMORE UZ eM/rc ATTORNEY l alz ented Nov; 24, 1970 Sheet g of 5 INVENTOR.
  • KEITH C STA/VSMORE UZ eM/rc ATTORNEY l alz ented Nov; 24, 1970 Sheet g of 5 INVENTOR.
  • KEITH C STA/VSMORE UZ
  • this invention is concerned with improvements in sedimentation apparatus or tanks of a type such as represented in the US. Pat. to Klopper, No. 3,295,835 of Jan. 3, 1967.
  • the Klopper type machine employs separate drive arms which have draft elements or ropes connecting them to what are light weight simple straight tubular rake arms which in turn are linked to the vertical shaft of the rake structure.
  • the Klopper machine avoids having complex or bulky girder arm structures operate in a sludge'thickening zone-and under direct heavy load, exposed to scaling and island formation.
  • These adverse conditions heretofore have not only necessitated frequent shutdowns for cleaning purposes, but they also have added greatly to the weight that must be supported by the bearing means of the rotating rake structure, while also adding to the amount of operating torque required.
  • These troublesome conditions are encountered for instance in the handling of heavy metallurgical sludges, and particularly they are troublesome in the thickening of the heavy viscous red'mud in the alumina industry.
  • This invention is concerned more particularly with improving the manner of introduction of the feed pulp into the Klopper machine, in view of problems due to the presence of the drive arm structure.
  • the object is to introduce into the feedwell a pair of streams directed into annular countercurrent paths located one above the other, in such a manner that the influent energy is dissipated or diffused, and the. feed pulp is distributed radially evenly in all directions, while entering the surrounding body of liquid undergoing sedimentation.
  • the invention utilizes a feedwell unit substantially of the type disclosed into U.S. Pat. No. 3,406,474 to Fitch.
  • This type of feedwell unit rapidly and completely dissipates the kinetic energy of a liquid stream or feed liquid entering a thickener or clariiier, into random turbulance of small scale eddies before entering the quiescent body of liquid undergoing sedimentation in the tank.
  • annular race ways of inwardly open annular channels are juxtaposed one above the other within a feedwell cylinder.
  • the main stream of the feed liquid is split into separate streams which are fed into these annular channels tangentially as well as counter'currently relative to each other, so that one stream rotates clockwise and the other counter clockwise, around the vertical axis of rotation of the rake structure.
  • These mutually opposed rotating streams are displaced inwardly into the open area surrounded by the channels, and are compelled to shear along the entire length of these channels at twice the velocity of either stream.
  • the stream velocities entering the feedwell are thereby instantaneously converted into random turbulence, and if the streams are made equal but oppositely directed, there are no residual tangential velocity components, so that a uniform flow velocity is obtainable across the area of the resulting stream passing from the feedwell radially outwardly in all directions into the quiescent body of liquid in the tank.
  • This mode of feed introduction improves the overall sedimentation efficiency ofthe tank.
  • the drive arm structure in the Klopper machine especially when located above the liquid level to avoid scale formation on the arms, creates a problem in respect to placing or mounting the aforementioned energy/dispensing type of feedwell unit in such a manner that it may operate effectively concentric with the vertical axis of rotation of the rake structure.
  • a stationary horizontal feed supply pipe or conduit leading into the feedwell would interfere withthe rotating parts such as the aforementioned draft elements of the rake structure.
  • this invention provides a feedwell arrangement combined and unitary with the rotating rake structure, featuring an exposed auxiliary feedwell located at an upper level, and a submerged feedwell located at a lower level, and receiving countercurrent streams of feed pulp from the upper level.
  • the rotating auxiliary feedwell in turn receives the feed pulp from a stationary duct.
  • the preferred energy dispersing type feedwell unit herein also termed the main feedwell may then be connected to, or integrated into the drive arm structure so as to be located below'said auxiliary annular feedwell, both the auxiliary feedwell and the main feedwell thus becoming unitary with the rotary rake structure.
  • Feed transfer duct or passage means supplythe feed pulp from the auxiliary feedwell to the annular inwardly open channels of the main feedwell, in such a manner as to maintain the two streams in the desired countercurrent energy dissipating annular paths.
  • the desired type feedwell may be used effectively irrespective of the presence and the position of the drive arm structure.
  • the two countercurrent streams may be introduced byway of elbow-shaped pipes located internally of the main feedwell, or else by way of external piping connected tangentially to the main feedwell cylinder.
  • FIG. I is a vertical, sectional view of a sedimentation tank having a rotary rake structure embodying one form of the feedwell construction of this invention, which has an auxiliary feedwell at an upper lever communicating with a main feedwell at a lower lever.
  • FIG. 1b is an enlarged view of details of the rake structure taken from FIG. 1.
  • FIG. la is a top view taken on line lb 1b in FIG. la.
  • FIG. 2 is an enlarged view of the feedwell construction taken from FIG. 1.
  • FIG. 3 is a cross section taken on line 3-3 in FIG. 2.
  • FIG. 4 is a cross section taken on line 4-4 in FIG. 2.
  • FIG. Si is a cross section taken on line 5-5 in FIG. 2.
  • FIG. 6 is a vertical, sectional view of the central portion ofa rotary rake structure, showing a modified feedwell construction of this invention, differing from FIG. 2.
  • FIG. 7 is a cross section taken on line 7-7 of FIG. 6.
  • FIGS. 8, 9 and 10 are diagrammatic renditions of the feedwell construction of FIG. 2, showing various modifications.
  • FIG. 11 is a diagrammatic rendition of the feedwell construction showing still another modification.
  • FIG. 12 is a plan view taken on line 12-12 in FIG. 11.
  • the sedimentation apparatus in the embodiment in FIGS. 1 to 5 is equipped with a rake structure 10 operating in a tank 11, and supported from an overhead structure or bridge 12 extending diametrically across the tank. Feed slurry or pulp is supplied to the tank through a feed supply pipe 13, while clarified liquor overflows into a peripheral launder 14, and sediment or sludge is conveyed by the rake structure over the tank bottom through a central collecting zone or sump 15 for withdrawal through a sludge discharge pipe 16.
  • the rake structure itself comprises a vertical shaft 17 depending from and rotated by a drive mechanism 18 mounted upon the bridge.
  • a pair of rake arms 19 and 20 are connected to the lower end portion of the shaft by means of a double bracket D, in such a manner as to be movable about a horizontal axis h-h, as well as about a vertical axis V-v (see also FIGS. 1a and lb).
  • the rake arms themselves are in the form of tubular members 190 and 20a respectively, to which are wcldedthe usual raking blades 1% and 20b respectively.
  • a pair of horizontal drive arms 21 and 22 is fixed to the upper portion of the shaft, so as to extend just above the overflow level L.
  • Each drive arm pulls an associated rake arm 7 against a sludge load on the bottom of the tank, through inclined draft elements or drag rope means 23 and 24 respectively. It will be seen that rotation of the shaft by the drive mechanism will cause the rake arms to move sludge over the tank bottom to the central collecting zone, while leaving them free to yield to undue sludge accumulations, by a compound movement about the horizontal and vertical axes.
  • a feed suspension or slurry or a pulp is supplied through feed pipe 13 to a feedwell construction 25 which according to the invention comprises an upper or auxiliary feedwell 26, and a lower or main feedwell 27, both built substantially concentric around the axis of rotation of the rake structure, although in this embodiment vertically spaced from each other by the drive arm structure.
  • the auxiliary feedwell is in the form of an annular trough fixed to the top side of the drive arm structure, while the main feedwell comprising a cylinder 28 is fixed to the underside.
  • Feed slurry received by the annular feedwell trough 26 is delivered into the main feedwell 27 through a pair of depending ducts or transfer pipes 29 and 29a terminating within the feedwell cylinder 27.
  • the shorter transfer pipe 29 of length 1-1 has an elbow shaped lower end portion directed for delivering a first stream of feed slurry substantially tangentially into an upper annular horizontal zone 2-] of the main feedwell.
  • the longer transfer pipe 29a of length 1-2 also has an elbow shaped lower end portion directed for delivering a second stream of feed slurry substantially tangentially into annular horizontal zone 2-2 of the main feedwell. These two annular streams are directed opposite to one another, operating in submergence, that is below the liquid level L.
  • the lower. zone 2-2 may be confined between an annular bottom shelf 30 and an intermediate shelf 31.
  • the upper zone Z-l may be confined between the intermediate annular shelf 31 and an annular top shelf or plate 32.
  • the two countercurrently rotating streams are subject to mutual shearing action in the central area surrounded by the zones Z-l and 2-2, with the result that the influent energy is dissipated, and the feed slurry enters the surrounding quiescent body of liquid uniformly distributed in all directions as indicated by arrows A.
  • the rake structure has a shaft 33 depending from, and supported by a drive unit 34 mounted upon a bridge structure indicated at 35.
  • a pair of rake arms 37 and 38 are similar to those above in FIG. I, including the manner in which they are connected to the shaft, allowing each rake arm to be movable about a horizontal and a vertical axis.
  • a pair of drive arms 39 and 40 associated with respective rake arms through draft elements or drag ropes (here not shown), is substantially submerged just below the liquid level L-2 in the tank, in order that a low roof structure 41 for the tank may be accommodated.
  • the drive arms are of girder type construction having a pair of parallel upper stringers 42 and d3 shown to be composed of flange-connected pipe sections, and a similar pair of parallel lower stringers 44 and 45, all stringers being interconnected by bracing members at the sides, the bottom, and the top.
  • the middle portion of the girder intermediate the ends is fixed to the shaft of the rake structure.
  • the upper pair of stringers are rigidly weld-connected to each other and to the shaft by means of an upper horizontal gusset plate 46 of square configuration.
  • a similar lower gusset plate 47 similarly interconnects the lower pair of stringers and the shaft.
  • the feedwell structure of FIGS. 6 and 7, while functionally similar to the one in FIG. I, has a main feedwell 49 integrated into, or horizontally penetrated by the drive arm girder structure just described, while an associated annular auxiliary feedwell 50 surrounding the shaft is fixed to the top side of the girder.
  • the upper auxiliary and the lower main feedwell are joined together substantially at the liquid level L-2, with the main feedwell properly positioned and submerged in the top zone ofthe liquid body in the tank.
  • a cylinder 51 ofthe main feedwell has inner annular shelves 52 and 53 defining a lower annular zone 2-4, and has an annular top plate 54 defining with shelf 53 an upper annular zone Z-S, the top plate also constituting the bottom of auxiliary feedwell 50.
  • a pair of depending feed transfer pipes 55 and 56 substantially in the manner of the FIG. I embodiment, supply countercurrently directed streams of feed slurry from the upper or auxiliary feedwell tangentially into respective annular zones 2-4 and 2-5. In this way, the influent energy is dissipated in the manner previously described, allowing the feed slurry to enter the surrounding body of quiescent liquid uniformly distributed in all directions as indicated by arrows B.
  • FIGS. 3, 9 and 10 while resembling the FIGS. 1 to 5 embodiment are diagrammatic renditions illustrating some of the modifications that come within the concept of the combination of the drive arms with an annular auxiliary feedwell located at an upper level, and a main feedwell located at a lower level, both feedwells rotating unitary with the rake structure, while streams of feed slurry are supplied from the auxiliary feedwell countercurrently and tangentially into an upper and a lower zone within the main feedwell.
  • the liquid level is indicated at L-3.
  • FIG. 8 while omitting the annular shelves from the cylinder of the main feedwell, shows two depending transfer pipes 57 and 58 delivering streams of the feed slurry countercurrently and tangentially into an upper and a lower annular zone designated at Z-6 and 2-7 respectively.
  • FIG. 9 adds to the FIG. 8 construction an annular bottom shelf 59 for downwardly confining the lower annular zone 2-8, the upper zone being designated as Z-9.
  • FIG. 10 adds to the bottom shelf 59 of the FIG. 9 construction a second annular shelf 60 spaced upwardly to provide an annular partition between the lower zone 2-10 and the upper zone Z-l1.
  • FIGS. 11 and 12 differs from the preceding embodiments in that the two countercurrent streams of feed slurry are introduced into their respective upper and lower zones 2-12 and Z-13 by means of pipes 62 and 63 having their inner ends connected tangentially to the outside of a main feedwell cylinder 64, and their outer ends connected toan annular auxiliary feedwell 65 having an outside diameter substantially larger than that of the main feedwell cylinder located below.
  • the invention as herein illustrated need not be limited to the depending type of rake structure supported from an overhead construction or bridge, but that the concept is applicable also to the initially mentioned center pier-supported type of rake structure, in which case a corresponding feedwell construction is built around and connected to the vertical central cage portion of the rake structure that surrounds the pier.
  • a continuously operating sedimentation tank having a supply of feed liquid, a bottom outlet zone for sludge and overflow means for liquid separated from the sludge, and determining the liquid level in the tank, the combination which comprises:
  • a rake structure mounted for rotation about avertical axis, effective to move sludge overthe tank bottom to'a sludge.
  • said rake structure comprising a central vertidrive arm structure
  • a main feedwell fixedly connected to said drive arms substantially concentric with said axis of rotation, and located below said auxiliary annular feedwell and in submergence,'and flow passage means constructed and arranged to deliver a pair of streams from said auxiliary feedwell into said main feedwell, said streams being directed into.
  • annual countercurrent paths located one above the other, in such a manner that the influent energy is dissipated, and the feed pulp is distributed radially evenly in all directions while entering the surrounding body of liquid undergoing sedimentation.
  • cal member bearing means at the upper end of said vertical member, supportingsaid member for rotation about said vertical axis, a plurality of rake arms extending from the lower end of said vertical member, a drive arm structure having a corresponding number of drive arms extending rigidly from the upper end portion of said vertical member, and draft elements connecting the outer end portions of said drive arms with said rake arms;
  • auxiliary annular feedwell receiving feed liquid in the form of an annular channel substantially concentric with said vertical axis and connected to the top side of said 7.
  • said main feedwell is connected to the underside of said drive arms and wherein at least one of said ducts extends from said auxiliary feedwell downwardly externally of said channel structure.
  • annular auxiliary feedwell has an inner diameter substantially greater than the diameter of said main feedwell, and wherein said flow passage means comprise conduits connected to said' main feedwell for introducing said streams tangentially into the respective annular paths.
  • said main feedwell comprises an internal annular bottom shelf downwardly confining the lower annular stream.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Treatment Of Sludge (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
US805568A 1969-03-10 1969-03-10 Sedimentation tank with rotary sediment raking structure Expired - Lifetime US3542207A (en)

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US80556869A 1969-03-10 1969-03-10

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US (1) US3542207A (enrdf_load_stackoverflow)
JP (1) JPS4727863B1 (enrdf_load_stackoverflow)
BR (1) BR7017360D0 (enrdf_load_stackoverflow)
DE (1) DE2010832C3 (enrdf_load_stackoverflow)
FR (1) FR2039579A5 (enrdf_load_stackoverflow)
GB (1) GB1300724A (enrdf_load_stackoverflow)
NL (1) NL160730C (enrdf_load_stackoverflow)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3933655A (en) * 1974-03-12 1976-01-20 Warman Equipment International Cable-controlled thickener
US3959152A (en) * 1973-12-28 1976-05-25 Dorr-Oliver Incorporated Traction-driven composite sludge raking mechanism for sedimentation tanks
US4000075A (en) * 1975-12-31 1976-12-28 Dorr-Oliver Incorporated Sedimentation tank with rotary yieldable rake arm structure
US4048076A (en) * 1975-12-29 1977-09-13 Environmental Elements Corporation Center column drive arrangement for circular clarifiers
US4172040A (en) * 1978-10-19 1979-10-23 Aluminiumipari Tervezo Es Kutato Intezet Sediment raking device
EP0010395A1 (en) * 1978-10-10 1980-04-30 Dorr-Oliver Incorporated Settling tank
US4367141A (en) * 1979-09-25 1983-01-04 Doeroemboezi Bela Apparatus for the concentration of sludges and suspensions
US5445173A (en) * 1994-07-18 1995-08-29 Matrix Service, Inc. System for stirring and thereby reducing build up of bottom sediments in a storage tank
WO1999037378A1 (en) * 1998-01-26 1999-07-29 Baker Hughes Incorporated Clarifier feedwell
US20040149639A1 (en) * 2002-11-15 2004-08-05 Weston Vaughn J. Apparatus for mixing and dispensing influent slurry into a tank and systems incorporating same
US20080110839A1 (en) * 2006-10-25 2008-05-15 Foreman Don J Thickener/clarifier feedwell assembly with froth dissipation

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012051536A1 (en) * 2010-10-14 2012-04-19 Flsmidth A/S Thickener/clarifier feedwell having volute peripheries

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3959152A (en) * 1973-12-28 1976-05-25 Dorr-Oliver Incorporated Traction-driven composite sludge raking mechanism for sedimentation tanks
US3933655A (en) * 1974-03-12 1976-01-20 Warman Equipment International Cable-controlled thickener
US4048076A (en) * 1975-12-29 1977-09-13 Environmental Elements Corporation Center column drive arrangement for circular clarifiers
US4000075A (en) * 1975-12-31 1976-12-28 Dorr-Oliver Incorporated Sedimentation tank with rotary yieldable rake arm structure
EP0010395A1 (en) * 1978-10-10 1980-04-30 Dorr-Oliver Incorporated Settling tank
US4172040A (en) * 1978-10-19 1979-10-23 Aluminiumipari Tervezo Es Kutato Intezet Sediment raking device
US4367141A (en) * 1979-09-25 1983-01-04 Doeroemboezi Bela Apparatus for the concentration of sludges and suspensions
US5445173A (en) * 1994-07-18 1995-08-29 Matrix Service, Inc. System for stirring and thereby reducing build up of bottom sediments in a storage tank
EP0697252A1 (en) 1994-07-18 1996-02-21 Matrix Service, Inc. A system for stirring and thereby reducing build up of bottom sediments in a storage tank
WO1999037378A1 (en) * 1998-01-26 1999-07-29 Baker Hughes Incorporated Clarifier feedwell
US20040149639A1 (en) * 2002-11-15 2004-08-05 Weston Vaughn J. Apparatus for mixing and dispensing influent slurry into a tank and systems incorporating same
US20080110839A1 (en) * 2006-10-25 2008-05-15 Foreman Don J Thickener/clarifier feedwell assembly with froth dissipation
US7547396B2 (en) * 2006-10-25 2009-06-16 Flsmidth Technology A/S Thickener/clarifier feedwell assembly with froth dissipation

Also Published As

Publication number Publication date
NL7003306A (enrdf_load_stackoverflow) 1970-09-14
BR7017360D0 (pt) 1973-03-08
DE2010832C3 (de) 1980-05-29
JPS4727863B1 (enrdf_load_stackoverflow) 1972-07-25
DE2010832B2 (de) 1979-09-13
GB1300724A (en) 1972-12-20
NL160730B (nl) 1979-07-16
DE2010832A1 (enrdf_load_stackoverflow) 1970-10-01
FR2039579A5 (enrdf_load_stackoverflow) 1971-01-15
NL160730C (nl) 1979-12-17

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Owner name: BANCBOSTON FINANCIAL COMPANY, ONE LANDMARK SQUARE,

Free format text: SECURITY INTEREST;ASSIGNOR:DORR VENTURES, INC., A DE CORP.;REEL/FRAME:004725/0170

Effective date: 19870430