US3552575A - Centrifuge - Google Patents

Centrifuge Download PDF

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Publication number
US3552575A
US3552575A US780531A US3552575DA US3552575A US 3552575 A US3552575 A US 3552575A US 780531 A US780531 A US 780531A US 3552575D A US3552575D A US 3552575DA US 3552575 A US3552575 A US 3552575A
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US
United States
Prior art keywords
bowl
centrifuge
annular
carrier
open top
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.)
Expired - Lifetime
Application number
US780531A
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English (en)
Inventor
Gunther Hultsch
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mannesmann Demag Krauss Maffei GmbH
Original Assignee
Krauss Maffei AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from DE19671632304 external-priority patent/DE1632304C3/de
Application filed by Krauss Maffei AG filed Critical Krauss Maffei AG
Application granted granted Critical
Publication of US3552575A publication Critical patent/US3552575A/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

Definitions

  • the remainder travels upwardly beyond the open top of the bowl and travels along the upwardly and outwardly sloping inner annular surfaces of rings in the secondary unit.
  • the solid fraction travels upwardly beyond the inner surfaces of successive rings.
  • the liquid fraction adheres to such surfaces and flows along convex top surfaces and thereupon along downwardly and outwardly sloping outer surfaces of the rings.
  • the present invention relates to centrifuges in general, particularly to continuous centrifuges for segregation of solid and liquid fractions in suspensions. Still more particularly, the invention relates to improvements in multistage centrifuges wherein a suspension or the like is subjected to a plurality of successive Separating actions.
  • Another object of the invention is to provide a continuous multistage centrifuge wherein the first or primary stage is readily removable from and reinsertable into the housing while the remaining stage or stages can remain in fully assembled condition.
  • a further object of the invention is to provide novel and improved means for supporting the stages of a multistage continuous centrifuge for suspensions or the like.
  • An additional object of the invention is to provide a cen trifuge which can be used for treatment of varioustypes of mixtures of solid and liquid fractions.
  • the improved centrifuge is particularly suited for separa-' tion of solid and liquid fractions of suspensions and comprises a rotary driving member which is provided with a preferably cylindrical hollow apertured carrier, a primary separating unit "including a perforated conical or semispherical bowl having an open top and being separably supported by and rotatable with the carrier (the bowl preferably extends into and may be fully accommodated in the interior of the hollow carrier), means for feeding incoming material into the bowl, preferably into the bottom zone of the bowl, whereby some of the liquid fraction passes through the perforations and the remainder of the material travels toward and beyond the open top of the bowl, and a secondary separating unit including at least one annular member which is preferably re'movably supported by annular surface, and a convex annular intermediate or top sur- 7 face disposed between the first and second annular surfaces.
  • the arrangement is such that, when the two units rotate, the solid fraction of the remainder of material which leaves the bowl travels upwardly along and beyond the first annular surface whereas the liquid fraction of the remainder adheres to and travels along .the first, intermediate and second annular surfaces to accumulate in a collecting chamber.
  • the carrier preferably rotates about a vertical axis and the cross-sectional area of the entire bowl, or of the major portion of the bowl, preferably increases toward the open top of the bowl.
  • FIG. 1 is a fragmentary axial sectional view of a centrifuge which embodies one form of my invention
  • FIG. 1 there is shown-a centrifuge which comprises a housing or casing 40 having a cylindrical shell 24 and a removable cover or top wall 30.
  • the latter is provided with a central opening for a feeding device 1 which supplies incoming material (e.g.,. a suspension of solid particles in a liquid carrier) into a perforated semispherical bowl'3bwhich forms part of a primary separating unit 3 in the centrifuge and is removably accommodated in a hollow cylindrical apertured carrier 12.
  • the bowl 3b has an open top andis reinforced by ring-shaped stiffening members or hoops 30.
  • stiffening members are preferably located in planes which are nonnal to the axis of a driving member 14, here shown as a shaft which is rigid with the bottom walll3 of the carrier 12.
  • the discharge end of the feeding device 1 preferably supplies incoming material into the bottom zone of the bowl 3b,-i.e., the outlet of the device 1 is preferably coaxial with the shaft 14. Some of the liquid fraction in the incoming material passes through the perforations of the revolving bowl 3b and through the aper; tures 15 of the carrier 12 to accumulate in a liquid collecting chamber 16 surrounded by the shell 24 of the housing 40.
  • a secondary separating unit 5 which comprises a series of annular members 4.
  • the lowermost or innermost annular member 4 is separably secured to the carrier 12 and is positioned in such a way that it intercepts the remainder of material which ascends above and beyond the open top of the bowl 3b.
  • Each such annular member has an' upwardly diverging first I annular surface 6 which receives material from the bowl 3b or from the preced- .ing ring 4, a second annular surface 7 which diverges (downwardly and outwardly) in a direction away from the corresponding annular surface 6, and an annular convex intermediate surface 8 which provides a gradual transition between the respective first and second surfaces 6 and 7.
  • annular members 4 rotate with the carrier 12, and the arrangement is suchthat the remainder of material leaving the open top of the bowl 3b moves against the first annular surface 6 of the lowermost annular member 4 whereby the solid fraction travels upwardly in response to rotation of the unit 5 and is propelled to reach the surface 6 of the next following annular member 4. Some of the liquid fraction adheres to the surface 6, thereupon to the surface S'and finally travels along the surface 7 of the lowermost annular member 4 to be discharged into the collecting chamber 16. Annular ramps 9 are interposed between successive annular members-4 to facilitate ascent of solid fraction and some liquid fraction from a lower annular surface 6 to the next following annular surface 6.
  • each ramp 9 defines with the adjoining convex annular surface 8 a narrow annular gap 10 fortheliquid fraction which flows along such surface 8 and onto the corresponding surface
  • the solid fraction which travels upwardly beyond the annular surface 6 of the uppermost annular member 4 is separated from the remainder of the liquid fraction as it travels along successive surfaces 6 and finally moves onto the platform of an annular evacuating member 11 to be discharged from a col- Iecting chamber 116 through one or more outlets 26 in the wall 24.
  • the means for separably coupling the bowl 3b to the carrier 12 comprises annular supporting members 17, 18 which are affixed to the bowl, and pins, bolts or analogous fasteners 19 which extend through the supporting members 17, 18 and are secured to the carrier. If desired, one of the supporting members l7, 18 can be secured to the carrier 12. The lower ends of the fasteners 19 extend into tapped bores provided in the bottom wall 13 of the carrier 12. The lowermost annular member 4 of the secondary separating unit 5 rests on and is secured to the upper edge portion 22 of the carrier 12. The annular members 4 of the unit 5 are secured to each other in such a way that they permit the liquid fraction to move beyond the surfaces 7 and into thecollecting' chamber 16. The latter has an outlet 28.
  • FIG. 2 illustrates u portion of a second centrifuge wherein the [)Illllllly squirming ⁇ lnll .l ht replaced by it different prima ry separating unit 2 which includes an upwardly diverging frustoconical bowl 217 reinforced by ring-shaped stiffening members or hoops 2a.
  • the angle alpha of divergence of the bowl 2b is constant all the way from the bottom wall 13 to the lowermost annular member 4.
  • the manner in which the bowl 212 is separably installed in and rotates with the carrier 12 is the same as or similar to that described in connection with FIG. 1 If desired, the bowl 2! can be held in the carrier 12 by snap action.
  • FIG. 3 shows a portion of a third centrifuge with a simpler secondary separating unit 5a which comprises a single annular member 4a.
  • the housing 40a comprises a removable cover or top wall 30a and a cylindrical shell 24a which accommodates two annular partitions 25, 27.
  • the partition 27 constitutes the bottom panel of the collecting chamber 160 for the liquid frac tion and the partition constitutes the bottom panel of a second collecting chamber 116a for the solid fraction.
  • the partition 25 slopes downwardly and outwardly so that the solid fraction is evacuated by gravity by way of an outlet 260.
  • a second outlet 28a is provided in the shell 24 directly above the partition 27 for evacuation of the liquid fraction.
  • the feeding device 1 extends through a seal in the top wall 30 and discharges incoming material (preferably a suspension) into the bottom zone of a semispherical bowl 312 which is identical with the bowl of FIG. 1.
  • the numeral 23 denotes an annular flange of the carrier 12a for the marginal portion of the bowl 3b and the numeral 22 denotes one of several fasteners which secure the marginal portion of the bowl to the baffle 20.
  • An antifriction bearing 29 surrounds the drive shaft 14 and is installed in the lower partition 27.
  • the shaft 14 drives the bottom wall 13a of the carrier.
  • the solid fraction is propelled beyond the upper edge of the surface 6 and accumulates in the chamber 1160 to be evacuated by way of the outlet 26a.
  • the outlet 28a serves to evacuate that part of the liquid fraction which enters the chamber 16a by way of the apertures 15 as well as the remainder of the liquid fraction which enters the chamber 16a by moving downwardly beyond the surface 7.
  • That portion of the bowl 3 which isimmediately adjacent to its open top is preferably a cylinder which is coaxial with the shaft 14.
  • the purpose of the primary separating unit 2 or 3 is to segregate from incoming material atleas't some liquid matter and to thereby enhance the operation of the secondary unit 5 or 5a. This is particularly desirable and advantageous when the solid fraction consistsof coarse or 'rnediurmsized particles of synthetic plastic material.
  • An important advantage of my'cent rifugeisthat the primary separating unit, or at least the bowl of theprirnary separating unit, can be rapidly and readily separated and removed from or reinstalled in the carrier 12 or 12a. Thisis' desirable when the centrifuge is to be used for treatment of different types of suspensions and the contents of one suspension" should not mix with the contents of the other suspension or suspensions. Furthermore, cleaning of the bowl can be carried out more readily if the latter is removed from the housing 40 or 40a.
  • the centrifugegcan be furnished with two or morebowls so that one bowl is being cleaned while the centrifuge is in use with another bowl.
  • the primary and secondary separating units are sepurably secured to the carrier 12 or 12a, this carrier takes up the weight of theseu'nits, i.e., the primary separating unit need not carry the secondary unit so that the primary unit can W employ a lightweight bowl which is just strong enough to take up stresses which arise under the action of material fed by the device 1.
  • the primary separating unit In many presently known centrifuges, the primary separating unit must be s trong enough to carry one or more secondary units.
  • Still another advantage of the improved centrifuge is that.
  • the carrier 12 or 12a can accommodate and'transmit motion to different types of bowls.
  • the type of bowl can be selected as a function of the composition of incoming material, not only as regards the shape of the bowl but also as regards the number and size of perforations.
  • the shape-(angle of divergence) of a conical bowl is preferably selected in such a way that it enables the solid fraction to rise which enters the bowl (in and beyond the open top with minimal resistance. Hollow semicylindrical bowls are preferred in many'instances because the inclination of the rising solid fraction withv reference to the axis of rotation changes continuously and gradually.
  • a hollow semispherical bowl resembles a cylinder, it accumulates a layer of coarser particles of solid fraction, i.e., the internal surface of such layer is uneven and accelerates the material which slides thereover so that such material rotates at the speed of the bowl when it enters the secondary separating unit.
  • Another advantage of a semicylindrical or similar bowl is that the kinetic energy of material which enters the bowl (in parallelism with the axis of rotation) is utilized for segregation of liquid fraction '
  • the stiffening rings 2a or 3a render it possible to employ a very lightweight bowl because they reinforce the bowl in the region where the perforated wall of the bowl must withstand considerable centrifugal forces and the pressure of incoming material.
  • the main purpose of the baffle 20 is to insure separation- 0f at least some liquid fraction in the primary unit 2 or 3, and also that the remainder of material is properly directed against the surface 6 of the first or lowermost annular member 4 or against the surface 6 of a single annular member 4a.
  • narrow clearance 21 guides the material which leaves the bowl 2b or 3b against the adjoining surface 6.
  • a centrifuge particularly for separation of solid and liquid fractions of suspensions, comprising rotary carrier means; a primary separating unit including a perforated bowl having an open top and being removably supported by and rotatable with said carrier means; means for feeding incoming material into said bowl whereby some of the liquid fraction passes through and the remainder of such material travels toward and beyond the open top of said bowl; and a secondary separating unit including at least one annular member supported by and rotatable with said carrier means.
  • said annular member having an upwardly diverging first annular surface arranged to intercept said remainder of the material, a second annular surface located downstream of and diverging in a direction away from said first surface, and a convex annular intermediate surface disposed between said first and second surfaces.
  • the solid fraction of said remainder being arranged to travel upwardly along and beyond said first surface and the liquid fraction of said remainder being arranged to adhere to and to travel along and beyond said first, intermediate and second surfaces.
  • a centrifuge as defined in claim 1 wherein said carrier means is provided with at least one aperture for escape of liquid fraction which enters said carrier means through said bowl.
  • Y 5 A centrifuge as defined in claim 1, wherein said bowl is of conical shape and diverges upwardly toward said open top as therealong in response to rotation of the bowl.
  • a centrifuge as defined in claim I wherein said bowl is rotatable about a substantially vertical axis and said primary separating unit further comprises stifi'ening means for said bowl.
  • said stiffening means comprises rings located in planes making right angles with said axis.
  • each of said ramps has a lower edge defining with the intermediate surface of the adjoining lower annular member an annular gap for the liquid fraction.

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  • Centrifugal Separators (AREA)
US780531A 1967-12-15 1968-12-02 Centrifuge Expired - Lifetime US3552575A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19671632304 DE1632304C3 (de) 1967-12-15 1967-12-15 Zentrifuge (Prallringzentrifuge)

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Publication Number Publication Date
US3552575A true US3552575A (en) 1971-01-05

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US780531A Expired - Lifetime US3552575A (en) 1967-12-15 1968-12-02 Centrifuge

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US (1) US3552575A (de)
FR (1) FR1593467A (de)
GB (1) GB1226649A (de)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3730343A (en) * 1970-03-04 1973-05-01 Wolf Ag R Method and apparatus for separating water from a mixture of a granular material and water
US4133770A (en) * 1977-11-03 1979-01-09 Fives-Cail Babcock Screen for a basket of a centrifugal separator
US4175040A (en) * 1978-08-28 1979-11-20 Continental Oil Company Centrifugal water oil separator
US4320006A (en) * 1979-01-16 1982-03-16 Taiyu Shoji Kabushiki Kaisha Centrifugal oil separator
US5879610A (en) * 1991-03-21 1999-03-09 The Whitaker Corporation Method of making an electrical connector
US20030036720A1 (en) * 2001-08-17 2003-02-20 Spencer Dudley W.C. Hemodialysis assembly and method
US20030155312A1 (en) * 2002-02-15 2003-08-21 Ivansons Ivars V. Spin-hemodialysis assembly and method
WO2009039291A2 (en) * 2007-09-19 2009-03-26 Holmes George A Centrifugal pellet dryer and dewatering assembly

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2422464A (en) * 1942-09-01 1947-06-17 Bartholomew Tracy Method and apparatus for separating liquid from solids by rotatably mounted means
US3276591A (en) * 1962-12-05 1966-10-04 Krauss Maffei Ag Apparatus for treating suspensions

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2422464A (en) * 1942-09-01 1947-06-17 Bartholomew Tracy Method and apparatus for separating liquid from solids by rotatably mounted means
US3276591A (en) * 1962-12-05 1966-10-04 Krauss Maffei Ag Apparatus for treating suspensions

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3730343A (en) * 1970-03-04 1973-05-01 Wolf Ag R Method and apparatus for separating water from a mixture of a granular material and water
US4133770A (en) * 1977-11-03 1979-01-09 Fives-Cail Babcock Screen for a basket of a centrifugal separator
US4175040A (en) * 1978-08-28 1979-11-20 Continental Oil Company Centrifugal water oil separator
US4320006A (en) * 1979-01-16 1982-03-16 Taiyu Shoji Kabushiki Kaisha Centrifugal oil separator
US5879610A (en) * 1991-03-21 1999-03-09 The Whitaker Corporation Method of making an electrical connector
US20030036720A1 (en) * 2001-08-17 2003-02-20 Spencer Dudley W.C. Hemodialysis assembly and method
US20030155312A1 (en) * 2002-02-15 2003-08-21 Ivansons Ivars V. Spin-hemodialysis assembly and method
US6852231B2 (en) 2002-02-15 2005-02-08 Denco, Inc. Spin-hemodialysis assembly and method
WO2009039291A2 (en) * 2007-09-19 2009-03-26 Holmes George A Centrifugal pellet dryer and dewatering assembly
WO2009039291A3 (en) * 2007-09-19 2009-05-07 George A Holmes Centrifugal pellet dryer and dewatering assembly

Also Published As

Publication number Publication date
GB1226649A (de) 1971-03-31
FR1593467A (de) 1970-05-25

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