EP1350570A2 - Freitragende Zentrifuge mit einem sich nach aussen erweiternden zweiten konischen Trommelabschnitt - Google Patents

Freitragende Zentrifuge mit einem sich nach aussen erweiternden zweiten konischen Trommelabschnitt Download PDF

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Publication number
EP1350570A2
EP1350570A2 EP03015100A EP03015100A EP1350570A2 EP 1350570 A2 EP1350570 A2 EP 1350570A2 EP 03015100 A EP03015100 A EP 03015100A EP 03015100 A EP03015100 A EP 03015100A EP 1350570 A2 EP1350570 A2 EP 1350570A2
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EP
European Patent Office
Prior art keywords
conical
bowl
section
screen
bowl section
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP03015100A
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English (en)
French (fr)
Inventor
Woon-Fong Leung
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Baker Hughes Holdings LLC
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Baker Hughes Inc
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Filing date
Publication date
Application filed by Baker Hughes Inc filed Critical Baker Hughes Inc
Priority claimed from EP98956098A external-priority patent/EP1083993A1/de
Publication of EP1350570A2 publication Critical patent/EP1350570A2/de
Withdrawn legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B3/00—Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering
    • B04B3/04—Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl

Definitions

  • This invention relates to a cantilever type centrifuge and more specifically to a cantilever screen-scroll type centrifuge.
  • Conical screen-scroll centrifuges have been used to dewater thickened slurries from 40-60% feed solids to 80-90+% solids (or 20-10% cake moisture).
  • such centrifuges comprise a scroll conveyor 10 surrounded by a screen basket 12 and disposed therewith in a housing 14.
  • Scroll conveyor 10 and screen basket 12 are cantilevered from a support 16 at one end.
  • conveyor 10 and screen basket 12 are operatively connected to a single input, dual output planetary gear box or a cyclo gear box 18 which is driven by a motor 20.
  • a feed pipe 22 extends into an open, free end of scroll conveyor 10 for delivering a thickened feed slurry thereto.
  • the feed slurry exits an opening (not shown) in a hub 24 of conveyor 10 and is deposited onto screen basket 12.
  • Solids 26 in the slurry are conveyed along an inner surface of screen basket 12 to a conical discharge 28 by a helical blade 30 of conveyor 12, while filtrate is discharged at 32 through screen basket 12.
  • FIG. 1B A simple cross-sectional schematic of the screen-scroll centrifuge of Fig. 1A is shown in Fig. 1B.
  • Feed slurry introduced via feed pipe 22 into a feed cone 34 of conveyor 10 is accelerated in the feed cone (arrows 36) so that when the slurry is laid onto a small diameter end 38 of screen basket 12, the slurry has acquired the proper G-force to effect filtration of the bulk liquid followed by dewatering (arrows 32) so that the remaining liquid trapped in the cake pores can be further released with time.
  • the dewatering process is facilitated by continuously thinner cake and an increasing higher centrifugal force as the cake moves toward discharge at a larger screen diameter 42.
  • Washing can be applied to remove the impurities in food, chemical, and mineral applications, wash liquid being introduced at small diameter 38 of conical screen basket 12 shortly after the feed zone.
  • the washed cake is ultimately dewatered at the larger screen diameter 42.
  • the screen drain filtrate (arrows 32) and the cake (arrow 44) are collected respectively in separate hoppers (not shown) for downstream processing.
  • Figs. 1A and 1B One key benefit of the cantilever screen scroll design as illustrated in Figs. 1A and 1B, is that both scroll conveyor 10 and screen basket 12 are opened at the front end of the machine. This allows the operator easy access to the rotating assembly for regular maintenance such as replacement of worn components (e.g. screen, worn and broken tiles, scroll, nuts and bolts), and removal of foreign objects trapped in the process streams, as well as regular visual inspection of the process during operation to assure satisfactory operation. Because the screen scroll centrifuge is a cantilever design, another advantage is that only a set of supporting bearings located at one end of the machine is required instead of two bearings associated with a horizontal end-to-end support. This minimizes significantly the overall cost of the machine.
  • the overhung moment from the pivot or support may limit the cantilever mass as well as the distance of cantilever mass from the pivoted bearing or support. This may also result in a rotational speed limitation owing to natural frequency considerations.
  • Another limitation of the screen-scroll-type centrifuge is that the feed has to be pre-thickened to 40-60% before introduction to the screen to remove a majority of the bulk liquid. This thickening can be achieved, for example, with hydrocyclones, thickening tanks or thickening screens upstream of the dewatering screen scroll.
  • both thickening and dewatering are combined in a single unit using a screen bowl centrifuge as shown in Fig. 2.
  • a solid-bowl configuration comprises a cylindrical bowl 46 followed by a conical beach 48 used for separation and thickening of the separated solids to form a cake.
  • a cylindrical screen 50 downstream of the conical beach is used to further dewater the cake to lower the moisture content thereof. Consequently, dilute feed with solids content by weight of 5-50% can be used. This is advantageous over the screen scroll where only thickened feed of 40+% is permissible.
  • the prior art centrifuge of Fig. 2 also includes a worm-type conveyor 52 for scrolling cakes solids along inner surfaces of bowl 46, beach 48, and screen 50.
  • Effluents are discharged from a clarifier pool 54 into a centrate discharge chamber or hopper 56 of a centrifuge casing 58.
  • Filtrate is discharged through screen 50 into a filtrate drainage chamber or hopper 60 of casing 58, while cake 62 is discharged into a solids discharge chamber or hopper 64.
  • a feed slurry is fed into a hub 66 of conveyor 52 via a feed pipe 68.
  • Conveyor 52 and bowl 46 are rotatably supported at opposite ends on bearings 70 and 72 and are differentially rotated via a gear unit 74.
  • a cylindrical screen section 76 is provided at a larger diameter than the diameters of a cylindrical solid bowl section 78 and a bowl section 80.
  • a first helical conveyor blade 82 conveys cake solids along inner surfaces of bowl section 78 and bowl section 80, while a second helical conveyor blade 84 conveys cake solids along an inner surface of screen section 76.
  • Conveyor blades 82 and 84 are rigid with a conveyor hub 86 and accordingly rotate at the same angular velocity which is slightly different from an angular velocity of screen section 76, bowl section 78 and bowl section 80.
  • An advantage of the design of Fig. 3 is that cake dewatering on screen section 76 is carried out at a higher G-force.
  • a disadvantage is that as the feed as laid abruptly onto screen 76, the feed is underaccelerated, i.e., the tangential speed of the feed is much less than that of screen 76 at a solid-body rotation. This difference in tangential speed results in slippage of the feed on the screen surface as the feed is being accelerated by the screen surface, thereby causing high wear on screen 76 especially for abrasive feed materials. Furthermore, it can be shown that the undesirable radial velocity of the feed stream increases at the expense of a lower tangential speed (conservation of angular momentum).
  • the unit includes a cylindrical bowl 90 and a conveyor 92 both rotatably cantilevered from a support located at the large diameter side of the machine. Because of this arrangement, in order to reduce the overhung bending moment, the length of the solid-bowl section 90 as well as the length of a cylindrical screen section 94 must be trimmed. The rotational speed of the machine may also limited owing to natural frequency considerations. These factors render the overhung shorter screen bowl design less effective with major disadvantageous results of lower throughput, wetter cake and dirtier effluent as compared to a regular screen bowl supported by two end-to-end bearings with the same diameter.
  • the present invention is directed to the problem of providing a new and improved cantilever type centrifuge wherein throughput and cake moisture are improved over a conventional cantilever centrifuge. More specifically, the present invention is directed to providing a cantilever screen bowl centrifuge with a relatively high throughput and a relatively low cake moisture content.
  • a centrifuge comprises, in accordance with the present invention, a support, a conveyor cantilevered from the support, and a solid bowl also cantilevered from the support.
  • the conveyor includes a conveyor hub cantilevered from the support, the solid bowl extending about the hub.
  • the solid bowl includes an integral first conical bowl section which tapers radially inwardly towards an axis of the conveyor and the bowl and which has a small diameter end.
  • the centrifuge further comprises a second conical bowl section cantilevered at least indirectly from the support, the second conical bowl section having an input end at the small diameter end of the first conical bowl section.
  • the second conical bowl section has an increasing diameter away from its input end.
  • the first conical bowl section and the second conical bowl section together define a heavy phase transport path having a first portion of decreasing diameter extending along the first conical bowl section towards the small diameter end thereof and a subsequent second portion of increasing diameter extending along the second conical bowl section away from the input end of the second conical bowl section
  • the second conical bowl section is a screen or conical basket section.
  • the centrifuge is a conical screen bowl centrifuge with a conical solid beach section and a conical screen or basket of increasing diameter.
  • the conical basket effects thin cake dewatering inasmuch as the cake is spread out at a larger screen circumference toward discharge. This benefit is enhanced by a higher G-force for dewatering as the cake is conveyed to a larger diameter.
  • the conical screen with a larger surface area compensates, in part, the short cylindrical screen as shown in the cantilever design of Fig. 4.
  • the cantilever centrifuge of the invention is assembled in three stages or steps.
  • the first-half of a cylindrical hub is mounted first, followed by the solid-bowl section and the conical basket.
  • the second-half of the scroll is installed to fit the conical basket. In all cases, the clearance between the blade tip and the conical bowl wall can be reduced to the desirable tolerance by axial alignment of the components.
  • the conical basket section is attached to the conveyor, and more particularly to a free or downstream end of the conveyor, for rotating at a common angular velocity therewith.
  • the conical basket section extends in an axial direction away from its input end and towards the machine support. Concomitantly, the conical basket section surrounds at least a portion of the solid bowl and particularly the conical bowl section thereof.
  • This preferred embodiment of the invention combines the full benefit of the solid bowl and the conical screen scroll. Because the conical screen turns back toward the support end of the machine, the overhung moment is reduced.
  • the screen bowl section can be made longer than in cantilever centrifuges where the screen extends away from the machine support.
  • the outer surface of the solid-bowl is provided with a set of conveyor blades turned in the same sense as the set of conveyor blades inside the solid bowl.
  • the solid bowl and the blades welded along its outer surface are rotated at a speed different from the rotation speed of the conveyor hub and the basket to thereby effect a continuous discharge and control of retention time of the solids in the solid bowl as well as in the basket.
  • a feed accelerator is disposed at the downstream end of the first conical bowl section for tangentially accelerating in the direction of rotation (as opposed to radially accelerating) a thickened feed of 40-60% solids moving from the downstream end of the first conical bowl section to the upstream end of the second conical bowl section.
  • the feed accelerator includes a vane extending outwardly from the passageway towards an inner surface of the second conical bowl section. This vane may have an outer end which is curved forward in the direction of rotation for providing an additional tangential velocity component (overspeed) to the thickened feed being delivered to the upstream end of the second conical bowl section.
  • a feed accelerator may also be disposed in the hub for tangentially accelerating a relatively dilute feed of 5-30% solids prior to delivering the feed from the hub to a slurry pool in the solid bowl, thereby providing the dilute feed with a rotation speed at least approximately equal to that of the solid bowl.
  • This feed accelerator eliminates slippage and turbulence of feed in the pool resulting in instantaneous G-field for separation of suspended solids in the pool.
  • the other feed accelerator, at the downstream end of the first conical bowl section eliminates slippage of thickened feed on the screen/basket at a larger diameter, thereby reducing wear, particle attrition from slippage on the screen, and loss of fine solids.
  • the instantaneous G-field allows best use of the screen area for bulk filtration. As a consequence, higher throughput with better quality product (drier cake, better solids recovery) is expected from both feed accelerators.
  • the second conical bowl section is provided at a free or downstream end with a cylindrical screen section.
  • the conveyor has a hub and plurality of generally axial vanes extending from the hub along a substantial portion of the solid bowl (clarifier) section, while the conveyor has a conveyor blade attached to radially outer edges of the vanes so that the blade extends only part of a distance from an inner surface of the solid bowl to the hub.
  • the conveyor blades are made of ribbon blade segments supported by the axial vanes. This structure of the conveyor improves rigidity while reducing the overhung mass.
  • the axial vanes when submerged in the liquid pool facilitate axial flow of the effluent liquid, which reduces entrainment of the sediment in the bowl, the sediment being conveyed along the helical channels formed by adjacent conveyor blades.
  • conventional solid blades can also be used with the blades attached to the conveyor hub.
  • the conical basket section is attached at an upstream end to the free or downstream end of the first conical bowl section and extends in an axial direction away from the first conical bowl section, the solid bowl, and the support.
  • a solids separation method in accordance with the present invention comprises (1) feeding a slurry, i.e., a relatively dilute feed composition, from a cantilevered conveyor hub outwardly to a clarifier pool in a cantilevered solid bowl of a centrifuge, (2) scrolling cake solids from the clarifier pool along a cantilevered inwardly tapered first conical bowl section to a cantilevered outwardly tapered second conical bowl section with a cake inlet end at a downstream end of the first conical bowl section, and (3) scrolling cake solids from the inlet end along the second conical bowl section so that the cake solids experience an ever increasing centrifugal force during continued travel along the second conical bowl section towards a cake discharge port.
  • a slurry i.e., a relatively dilute feed composition
  • the method further comprises centrifugally draining filtrate from the cake solids on the section conical bowl section through the filter screen.
  • the second conical bowl section is rotated at a common angular velocity with the conveyor hub and a conveyor blade attached thereto.
  • the second conical bowl section is attached at an upstream end to a free or cantilevered end of the conveyor hub and surrounds at least a portion of the first conical bowl section and the solid bowl.
  • the scrolling of cake solids along the second conical bowl section including scrolling cake solids towards a supported end of the solid bowl and is implemented by turning an additional conveyor blade attached to an outer surface of the first bowl section, the additional conveyor blade being turned at a common angular velocity with the first conical bowl section.
  • a cantilever centrifuge with a screen bowl section overlapping a solid beach section and a solid bowl clarifier section in accordance with the present invention provides a heavy-duty inexpensive design with key benefits being its compact size and its easy accessibility. For the same footprint, this overlapping-type design has more screen area and a solid bowl clarifier section as compared to existing designs.
  • a cantilever centrifuge with a screen bowl section overlapping a solid beach section and a solid bowl clarifier section in accordance with the present invention accepts dilute feed stream and obviates the prethickening equipment which is normally used for this application.
  • the unique design allows higher solids throughput, drier cake, and superior recovery. It is a combination of a solid-bowl and a screen-scroll/conical- horizontal screen, all in one compact design.
  • a cantilever conical screen bowl centrifuge comprises a scroll- or worm-type conveyor 100 and a bowl 102 both rotatably cantilevered from a machine support 104.
  • Bowl 102 includes a substantially cylindrical solid bowl section 106 which extends about a hub 108 of conveyor 100.
  • Bowl 102 further includes a solid first conical bowl section 110 connected in cantilever fashion from a free or downstream end of solid bowl section 106 disposed opposite the machine support 104.
  • Conical bowl section 110 functions as a beach and tapers inwardly towards an axis 112 of conveyor 100 and bowl 102, in a downstream direction away from solid bowl section 106 and machine support 104.
  • a second conical bowl section 114 in the form of a conical screen or basket is connected at an upstream end to a free or downstream end of solid conical bowl section 110 opposite the solid bowl section.
  • Conical basket 114 tapers outwardly from rotation axis 112 in a direction away from the free or downstream end of conical bowl section 110.
  • Conveyor 100 includes multiple helical blades 116 which, in the region of solid bowl section 106, are attached to radially outer edges of a plurality of axially extending vanes 118 rigid with conveyor hub 108. Conveyor blades 116 extend only part of a distance an inner surface of solid bowl section 106 to hub 108 and are made of ribbon blade segments supported by vanes 118. This structure of conveyor 100 improves rigidity while reducing the overhung mass. Vanes 118, when submerged in a liquid clarifier pool 120, facilitate an axial flow of the effluent liquid, which reduces entrainment of the sediment in the bowl, the sediment being conveyed along the helical channels formed by adjacent conveyor blades.
  • a feed pipe 122 extends into hub 108 for delivering thereto a relatively dilute feed composition including 5-50% solids.
  • Conveyor 100 is provided with a feed accelerator 124 mounted to hub 108 for providing the incoming feed composition with a tangential velocity substantially equal to the tangential velocity of the slurry at the radially inner surface of clarifier pool 120.
  • Accelerator 124 includes a distributor 126 which receives the incoming feed composition and directs it to a plurality of feed openings or passageways 128 in hub 108.
  • Distributor 126 may be formed with a plurality of axially extending vanes (not shown) for imparting some measure of tangential velocity to the feed composition prior to the exit of the feed composition through feed openings 128.
  • Accelerator 124 further includes a plurality of anti-Coriolis baffles 130 extending inwardly into hub 108 at respective feed openings 128.
  • accelerator 124 may include a plurality of vanes (not shown) extending outwardly from respective feed openings 128 and, optionally, one or more smoothening elements (not shown) located between feed openings 128 and clarifier pool 120 for spreading out the feed stream from each opening 128. All of these features are described in detail in U.S. Patents Nos. 5,551,943, 5,632,714, and 5,520,605, the disclosures of which are hereby incorporated by reference.
  • the cantilever conical screen bowl centrifuge of Fig. 5 is assembled in three stages or steps.
  • a first-half 148 of hub 108 together with connected conveyor blades (not separately designated) is mounted first, followed by solid-bowl section 106 with conical beach section 110, and subsequently by conical basket 114.
  • a second-half of the scroll or conveyor blades is installed to fit conical basket 114.
  • another cantilever conical screen bowl centrifuge comprises a scroll- or worm-type conveyor 150 and a solid bowl 152 both rotatably cantilevered from a machine support 154 which includes a gear box, bearings, motor and sheave (none illustrated).
  • Bowl 152 includes a substantially cylindrical solid bowl section 156 which extends about a hub 158 of conveyor 150.
  • the solid bowl section 156 can also be substantially conical with the large diameter facing the support (see Figs. 11 and 12).
  • Bowl 152 further includes a solid first conical bowl section 160 connected in cantilever fashion from a free or downstream end of solid bowl section 156 disposed opposite the machine support 154.
  • Conical bowl section 160 functions as a beach and tapers inwardly towards an axis 162 of conveyor 150 and bowl 152, in a downstream direction away from solid bowl section 156 and machine support 154.
  • a second conical bowl section 164 in the form of a conical screen or basket is connected at an upstream end to a free or cantilevered end of conveyor hub 158, opposite machine support 154.
  • basket 164 rotates at the same angular velocity as hub 158, which is different from the angular velocity of solid bowl section 156 and conical beach section 160.
  • Conical basket 164 tapers outwardly from rotation axis 162 in a downstream direction, away from the free or cantilevered end of hub 158.
  • Conveyor 150 includes multiple helical blades 166 which, in the region of solid bowl section 156, are attached to radially outer edges of a plurality of axially extending vanes 168 rigid with conveyor hub 158. Conveyor blades 166 extend only part of a distance from an inner surface of solid bowl section 156 to hub 158 and are made of ribbon blade segments supported by vanes 168. The advantages and functions of vanes 168 are discussed above with reference to vanes 118.
  • a feed pipe 172 extends into hub 158 for delivering thereto a relatively dilute feed composition including 5-50% solids.
  • Conveyor 150 is provided with a feed accelerator 174 mounted to hub 158 for providing the incoming feed composition with a tangential velocity substantially equal to or greater than the tangential velocity of the slurry at the radially inner surface of a clarifier pool 170.
  • Accelerator 174 includes a distributor 176 which receives the incoming feed composition and directs it to a plurality of feed openings or passageways 178 in hub 158.
  • Distributor 176 may be formed with a plurality of axially extending vanes (not shown) for imparting some measure of tangential velocity to the feed composition prior to the exit of the feed composition through feed openings 178.
  • Accelerator 174 further includes a plurality of anti-Coriolis baffles 180 extending inwardly into hub 158 at respective feed openings 178.
  • accelerator 174 may include a plurality of vanes (not shown) extending outwardly from respective feed openings 178 and, optionally, one or more smoothening elements located between feed openings 178 and clarifier pool 170 for spreading out the feed stream from each opening 178.
  • a plurality of conveyor blades or helical scrolling elements 182 are attached to an outer surface of conical bowl or beach section 160 and to an outer surface of solid bowl section 156 for scrolling cake solids along an inner surface of conical bowl section or basket 164 to an end-type cake discharge opening 184, as indicated by arrows 186.
  • Conveyor blades or scrolling elements 182 are turned in the same sense as conveyor blades 166 inside solid bowl 152.
  • Solid bowl section 156 and conical bowl or beach section 160, as well as blades or scrolling elements 182 welded along the outer surfaces thereof, are rotated at a speed different from rotation speed of conveyor hub 158 and basket 164 to thereby effect a continuous discharge and control of retention time of the solids in solid bowl section 156 as well as in basket 164.
  • Conical basket 164 effects thin cake dewatering inasmuch as the cake is spread out at a larger screen circumference toward cake discharge rim or lip 142 and 184. This benefit is enhanced by a higher G-force for dewatering as the cake is conveyed to a larger diameter.
  • the cantilever centrifuge of Fig. 6 is assembled in three stages or steps.
  • hub 158 together with conveyor blades 166 is mounted to machine support 154 and particularly to a first drive shaft 155 which is connected to the spline shaft 155a of the gear box.
  • solid-bowl section 156 and conical bowl or beach section 160, together with conveyor blades or scrolling elements 182 are mounted to machine support 154 (gear housing, bearings, casing, motor and sheave) and particularly to a second drive shaft 157 thereof.
  • conical basket 164 is attached to the free or cantilevered end of hub 158.
  • the clearances between the conveyor blades 166 and the inner surfaces of solid bowl section 156 and conical beach section 160 and between conveyor blades or scrolling elements 182 and the inner surface of conical bowl section or basket 164 may be controlled by axial adjustment of the mounting components.
  • conical bowl section or basket 164 surrounds at least a portion of conical bowl or beach section 160 and solid bowl section 156. Because conical bowl section or basket 164 turns back toward machine support 154, the overhung moment is reduced. Conical bowl section or basket 164 can be made longer than in cantilever centrifuges where the screen extends away from the machine support.
  • An additional cylindrical screen section 188 may be connected to the downstream end of conical bowl section or basket 164.
  • a respective plurality of conveyor blades or helical scrolling elements 189 are attached to an outer surface of solid bowl section 156 for scrolling cake solids along an inner surface of cylindrical screen section 188 to a cake discharge opening (not designated), as indicated by a dashed arrow.
  • Conveyor blades or scrolling elements 189 are also turned in the same sense as conveyor blades 166 inside solid bowl section 156.
  • the addition of cylindrical screen extension 188 serves to increase the retention time needed for cake washing as well as dewatering.
  • the centrifuge of Fig. 6 has an additional feed accelerator 190 which is disposed at the downstream end of conical bowl section or beach 160 for tangentially accelerating a thickened feed of 40-60% solids moving from the downstream end of conical bowl section 160 to the upstream (small diameter) end of basket 164.
  • feed accelerator 190 is provided at the downstream end of beach 160 at a feed opening or passageway 192 provided for guiding the thickened feed from beach 160 to basket 164.
  • feed accelerator 190 generally includes a vane 196 (Fig. 8) extending outwardly from passageway 192 towards an inner surface of basket 164.
  • Vane 196 is optionally provided with an outer end 198 which is curved forward in the direction of rotation for providing an additional tangential velocity component (overspeed) to the thickened feed being delivered to the upstream end of basket 164.
  • Feed accelerator 190 may also include a smoothening element 200 for spreading the thickened feed out along a greater area of basket 164.
  • feed accelerator 190 may include side walls (not shown) to contain the flow of heavy phase as the heavy phase is accelerated radially outwardly. The side walls together with the surface 196 forms a U-shaped channel.
  • U.S. Patents Nos. 5,551,943, 5,632,714, and 5,520,605, incorporated by reference herein, discuss the operation and structure of the various components of feed accelerator 190. Adapting the accelerator components of those disclosures to feed accelerator 190 is a routine matter for one skilled in the art.
  • Fig. 7 depicts a cantilever conical screen bowl centrifuge virtually identical to that of Fig. 6 except that heavy phase passes from conical bowl section 160 to the upstream end of conical screen bowl section 164 via a side opening or passageway 220 rather than an end opening or passageway 192.
  • the centrifuge of Fig. 7 includes a feed accelerator 216 consisting essentially of a vane 218 extending circumferentially and radially outwardly from a passageway or opening 220 in conical bowl section 160.
  • the assembly of the centrifuge of Fig. 7 is virtually identical to the assembly of the centrifuge of Fig. 6. Reference numerals used in Fig. 7 correspond to those used for the same elements in Fig. 6.
  • conveyor leads for example, double, triple or quadruple leads
  • blades 116, 166, and 182 are used herein to reduce the cake height effecting dewatering via drainage in basket sections 114 and 164. This also reduces the entrainment of the sediment in clarifier pools 120 and 170 for solid bowl sections 106 and 156. All wear prone areas of conveyors 100 and 150, bowls 106 and 156 and screen/baskets 114 and 164 are protected by wear resistant materials such as tungsten carbide, silicone carbide, ceramic, hard-facing or other wear resisting coating materials.
  • the cake can also be washed at the small diameter or upstream ends of baskets 114 and 164.
  • An important advantage is that the basket size can be identical to that of a regular screen-scroll without compromise. This makes it easy to retrofit an existing screen scroll centrifuge, such as shown in Figs. 1A and 1 B, to incorporate the design of Figs. 6 and 7. Thus, the prethickener equipment of the screen scroll centrifuge can be eliminated. It is to be noted that the lengths of solid bowl sections 106 and 156 as well as baskets 114 and 164 in Figs. 6-7 can be significantly greater than those of Figs. 4 and 5 because the center of mass of the rotating assembly is closer to the cantilever supports 104 and 154.
  • the centrifuge of Figs. 6 and 7 has a further advantage that the G-field is greater at a larger diameter as compared to the prior art shown in Fig. 4 and without the wear associated with the abrupt discharge of the thickened material to a larger screen diameter as shown in Fig. 3.
  • another cantilever conical screen bowl centrifuge comprises a scroll- or worm-type conveyor 250 and a solid bowl 252 both rotatably cantilevered from a machine support 254 which includes a gear box, bearings, motor and sheave (none illustrated).
  • Bowl 252 includes a substantially cylindrical solid bowl section 256 which extends about a hub 258 of conveyor 250.
  • Bowl 252 further includes a solid first conical bowl section 260 connected in cantilever fashion from a free or downstream end of cylindrical solid bowl section 256 disposed opposite the machine support 254.
  • Conical bowl section 260 functions as a beach and tapers inwardly towards an axis 262 of conveyor 250 and bowl 252, in a downstream direction away from solid bowl section 256 and machine support 254.
  • a second conical bowl section 264 in the form of a conical screen or basket is drivingly secured at a downstream end to conveyor hub 258 via a spider support 248.
  • Screen or basket 264 is rotatably mounted at an upstream end to a free or cantilevered end of conveyor hub 258 via a cantilevered extension 246 of conical bowl section 260 and a pair of bearings 244 and 242.
  • basket 264 rotates at the same angular velocity as hub 258, which is different from the angular velocity of solid bowl section 256 and conical beach section 260.
  • Conical basket 264 tapers outwardly from rotation axis 262 in a downstream direction, away from the free or cantilevered end of hub 258 and toward machine support 254.
  • Conveyor 250 includes multiple helical blades 266 which, in the region of solid bowl section 256, are attached to radially outer edges of a plurality of axially extending vanes 268 rigidly attached to conveyor hub 258. Conveyor blades 266 extend only part of a distance from an inner surface of solid bowl section 256 to hub 258 and are made of ribbon blade segments supported by vanes 268. The advantages and functions of vanes 268 are discussed above with reference to vanes 118.
  • a feed pipe 272 extends into hub 258 for delivering thereto a relatively dilute feed composition including 5-50% solids.
  • Conveyor 250 is provided with a feed accelerator 274 mounted to hub 258 for providing the incoming feed composition with a tangential velocity substantially equal to or greater than the tangential velocity of the slurry at the radially inner surface of a clarifier pool 270.
  • Accelerator 274 includes a distributor 276 which receives the incoming feed composition and directs it to a plurality of feed openings or passageways 278 in hub 258.
  • Distributor 276 may be formed with a plurality of axially extending vanes (not shown) for imparting some measure of tangential velocity to the feed composition prior to the exit of the feed composition through feed openings 278.
  • Accelerator 274 further includes a plurality of anti-Coriolis baffles 280 extending inwardly into hub 258 at respective feed openings 278.
  • accelerator 274 may include a plurality of vanes (not shown) extending outwardly from respective feed openings 278 and, optionally, one or more smoothening elements located between feed openings 278 and clarifier pool 270 for spreading out the feed stream from each opening 278.
  • a plurality of conveyor blades or helical scrolling elements 282 are attached to an outer surface of conical bowl or beach section 260 and to an outer surface of solid bowl section 256 for scrolling cake solids along an inner surface of conical bowl section or basket 264 to a cake discharge opening 284, as indicated by an arrow 286.
  • Conveyor blades or scrolling elements 282 are turned in the same sense as conveyor blades 266 inside solid bowl 252.
  • Solid bowl section 256 and conical bowl or beach section 260, as well as blades or scrolling elements 282 welded along the outer surfaces thereof, are rotated at a speed different from rotation speed of conveyor hub 258 and basket 264 to thereby effect a continuous discharge and control of retention time of the solids in solid bowl section 256 as well as in basket 264.
  • the centrifuge of Fig. 9 has an additional feed accelerator 290 which is disposed at the downstream end of conical bowl section or beach 260 for tangentially accelerating a thickened feed of 40-60% solids moving from the downstream end of conical bowl section 260 to the upstream (small diameter) end of basket 264.
  • feed accelerator 290 is provided at the downstream end of beach 260 at a feed opening or passageway 292 provided for guiding the thickened feed from beach 260 to basket 264.
  • Feed accelerator 290 generally includes a vane 296 extending outwardly from passageway 292 towards an inner surface of basket 264. That vane is optionally provided with an outer end (198 in Fig.
  • Feed accelerator 290 may additionally include a smoothening element (200 in Fig. 8) for spreading the thickened feed out along a greater area of basket 264 or, alternatively, the basket location where the feed is introduced can serve as a smoothener for the feed.
  • Fig. 10 depicts a cantilever conical screen bowl centrifuge virtually identical to that of Fig. 9 except that conical screen bowl section 264 has been replaced by a conical screen bowl section 316 and a cylindrical screen bowl section 314.
  • Conical screen bowl section 316 is substantially co-extensive with conical bowl section 264 in an axial direction, while cylindrical screen bowl section 314 is nearly coextensive with cylindrical bowl section 256.
  • Conveyor blades 282 are modified at 318 to extend to an inner surface (not labeled) of cylindrical screen bowl section 316.
  • Fig. 11 also depicts a cantilever conical screen bowl centrifuge virtually identical to that of Fig. 9 except that solid bowl sections 256 and 260 have been replaced by a single solid conical bowl section 320.
  • Solid bowl section 320 and screen bowl section 264 are substantially co-extensive with one another in an axial direction.
  • Conveyor blades 266 are modified at 322 so that the outer ends or edges of the conveyor blades extend to an inner surface (not labeled) of solid bowl section 320.
  • conveyor blades 282 are shortened at 323.
  • Fig. 12 illustrates a modification of the centrifuge of Fig. 7 wherein cylindrical solid bowl section 156 and conical bowl section 160 are replaced by a single solid conical bowl section 324.
  • Conical basket 164 is fixed at an upstream end to a cantilevered end of conveyor hub 158 via a flange 326. Thus, basket 164 rotates at the same angular velocity as hub 158.
  • Bowl section 324 is mounted for rotation about axis 162 at an angular speed slightly different from that of hub 158.
  • Conveyor blades 166 and 182 (Fig. 7) are replaced by helical conveyor blades 326 and 328 conforming to the modified bowl design.
  • Conveyor blades 328 extend the entire radial distance between conveyor hub 158 and the inner surface (not designated) of solid bowl section 324. As shown in Fig. 13, each wrap of conveyor blades 326 is provided with four to six circumferentially equispaced elliptical openings 330 to permit effluent to flow axially near the surface of a clarifier pool 332. This avoids a flow of high velocity effluent liquid through the helical channels of the conveyor blades 326, which would entrain the settled solids in the cake. Dilute feed after properly accelerated by feed accelerator 174 discharges into clarifier pool 170 for separation.
  • An advantage of the embodiment of Fig. 12 is that clarifier pool 332 has an increased volume relative to pool 170, thus facilitating sedimentation.
  • the design of Fig. 12 is relatively compact and space efficient.
  • the height and mass of the outer conveyor blades 328 are reduced relative to the design of Fig. 7, thus reducing the overall conveyor mass.
  • conical solid bowl sections and the conical screen bowl sections disclosed herein may each include multiple conical bowl sections extending at different angles relative to the axis of the machine.
  • cylindrical screen section 188 in Fig. 7 may be alternatively formed as a conical section having a cone angle different from that of conical screen bowl section 164.
  • cylindrical screen bowl section 314 in Fig. 10 may be replaced by another conical screen bowl section having an angle of inclination different from that of conical screen bowl section 316.

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  • Centrifugal Separators (AREA)
EP03015100A 1998-06-03 1998-10-08 Freitragende Zentrifuge mit einem sich nach aussen erweiternden zweiten konischen Trommelabschnitt Withdrawn EP1350570A2 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US8782498P 1998-06-03 1998-06-03
US87824P 1998-06-03
EP98956098A EP1083993A1 (de) 1998-06-03 1998-10-08 Freitragende zentrifuge mit einem sich nach aussen erweiternden zweiten konischen trommelabschnitt

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
EP98956098A Division EP1083993A1 (de) 1998-06-03 1998-10-08 Freitragende zentrifuge mit einem sich nach aussen erweiternden zweiten konischen trommelabschnitt

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EP1350570A2 true EP1350570A2 (de) 2003-10-08

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP03015100A Withdrawn EP1350570A2 (de) 1998-06-03 1998-10-08 Freitragende Zentrifuge mit einem sich nach aussen erweiternden zweiten konischen Trommelabschnitt

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EP (1) EP1350570A2 (de)

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