US832191A - Centrifugal separator. - Google Patents

Centrifugal separator. Download PDF

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US832191A
US832191A US26870505A US1905268705A US832191A US 832191 A US832191 A US 832191A US 26870505 A US26870505 A US 26870505A US 1905268705 A US1905268705 A US 1905268705A US 832191 A US832191 A US 832191A
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screw
drum
discharge
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centrifugal separator
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Wilhelm Holzer
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges 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
    • B04B2001/2058Centrifuges 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 with ribbon-type screw conveyor

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  • This invention relates to a device for separating mixtures of bodies in a continuous manner and with the aid of the centrifugal force.
  • This device may be used for mixtures of difl'erent composition,as well as for different kinds of separation.
  • solid bodies. of different natures contained in a mixture may be separated one from the other.
  • solid or muddy parts may be separated from a mixture composed chiefly of liquid.
  • liquids adhering to solid bodies may be separated from the latter.
  • Figure 1 is a section of the device, some of the internal parts being shown in side elevation.
  • Fig. 2 is a section on line a b of Fig. 1.
  • Fig. 3 shows a section on line 7c Z of the same figure.
  • Fig. 4 shows a modification of the device shown in Fig. 1, this figure being a section on lines f g h i of Fig. 5.
  • Fig. 5 shows a section on line 0 b of Fig. 4.
  • This shaft 6 is rotatably supported in its lower part (not shown) and carries fixed upon it the screw 4, as well as the parts secured to the latter-
  • the screw 4 leaves near its axis a hollow space or core through which the stationary pipe 3 projects in the centrifugal apparatus.
  • stiffening webs or stays 2.5 are provided, which are rigidly secured to the screw 4 or cast in one piece with the latter. These stiffening-stays are arranged round the inner opening of the screw 4, as shown by Fig. 3. They are only shown on both sides in Figs. 1 and 4 for sake of clearness.
  • Fig. 3 these rakes also exist in a certain number, only two rakes being shown in Fig. 1 on both sides of the worm 1n order to not complicate the drawings.
  • the screw 4 carries at its upper end, either rigidly secured to it or cast integral with it, first a spirally-wound share 16, then above this a circular plate 22, and above the latter a second spirally-wound share 18.
  • Plate 22 produces separate chambers for the shares 16 and 18.
  • the top of the mantle 5 is closed by a cover which is provided with a funnelshaped opening 17 and an annular opening 19 surrounding the latter.
  • the funnel may as well be made of one piece with the screw 4 and project through the cover of the cen-- trifugal separator.
  • Fig. 4 shows a narrower screw 4 and only one share 18*, another modification consisting in that the discharge-channels 17 a are rigidly connected to the screw 4 or made integral with the latter. Furthermore, these discharge-channels 19 are arranged on the same area of a circle and form a sort of cell upon the latter. In this instance the interval between the cellular channels 17 a and the-cover 0r mantle of the The exhaust-openings are arranged at different heights.
  • the discharge-channels 17 are cylindrical. However, they may also be conical when the nature of the material to be treated requires it. The same remarks may be made on behalf of the connecting-pieces of the shares.
  • the mantle 5, as well as the shaft 6, is pro vided with a drivingdevice which may have the most'varying forms and which for this reason is not shown inthe drawings.
  • the function of thedevice is as follows: Assuming that a mixture is to be treated which is composed of different kinds of solid bodies which are to be separatedone from the other, the mixture introduced by the charging device (not shown) falls through the tube 3 uniformly on the bottom of the rotating centrifugal apparatus, where it is thrown againstthe wall of the latter by reason of the centrifugal force: As the pipe 3 does not rotate, th'ere is no danger of the mixture adhering 'to-the wall of the tube. The screw 4 ro tates in the same direction as the mantle 5 of the centrifugal apparatus, but with a different speed.
  • the motion of the screw 4 ismore rapid or less rapid than the motion of the centrifugal "apparatus. It results from this difference'of speed between the centrifugal apparatus 5 and the screw 4 a raising motionof therniXed material which forms an annular couchalong the periphery of the separator. During its ascensional motion of the mixed material it is'continuously loosened and liftedoff the periphery, so that the heavier particles-can arrive n'ear the periphery and-push the'lighter particles more toward the center. In this manner :thebodies of the same kind will during their raising motion accumulate in annular 'COL1Ch6S,"tl16 lighter bodies-lying nearer to the center, while. the
  • the mantleof the centrifugal apparatus is enlarged at the top in orderto facilitatethe raising motion of the material.
  • the. enlargement of the mantle must only be sufficient to keep the upward motion .of the material in dependence of the relative motion of.the-sc.rew4..
  • I J According tothe nature of the material vto be treated the process is somewhatmodiiied.
  • the rake 15 may be dispensed with.
  • one of the shares may be omitted, as the liquid escapes quite automatically in proportion as fresh liquid is introduced through the tube 3.
  • the mantle of the apparatus may receive the form of a sieve and a less-importtant number of rakes may be made to slide along the periphery in order to keep the holes of the sieve open and the mass loose. The liquid may thus escape freely.
  • the liquid to :be separated is first projected against the periphery of the centrifugal apparatus, while the solid material is raised by the screw.
  • the liquid partly by gravitation, partly by the influence of the centrifugal force, flows downwardly in the material loosened and kept permeable by the rakes along the wall inclined obliquely downward and outward.
  • the liquid escapes at the lower end through special openings.
  • a centrifugal separator comprising a stationary feed-pipe, a rotatable conical drum provided with discharge-openings, a screw rotatable independently of the drum, and a plurality of fingers projecting outwardly from opposite sides of the blades of said screw to the drums.
  • a centrifugal separator comprising a stationary feed-pipe, a rotatable conical drum provided with centrally-disposed discharge-openings, a screw rotatable independently of the drumand provided with blades .drum provided with centrally-disposed :dis-
  • a centrifugal separator comprising a stationary feed-pipe, a rotatable conical drum, a screw'rotatable independentlyofathe drum, a plurality of fingers projecting radially from the blades of said screw,:and spiral shares 16 and 18 cooperating with theidelivery end of said screw.
  • a centrifugal separator comprisinga rotatable drum, feeding means delivering to the lower end of said-drumand aidischargeiat the upper end thereof, an independently-rotatable screw, and a share cooperating with said screw anddelivering to saiddischarge.
  • a centrifugalseparator comprisingarotatable drum, feeding means delivering to the lower end of said drum and a-disc'harge at the upper end thereof, an independently-rotatable screw, and a spiral share cooperating with said screw and delivering to said discharge.
  • a centrifugal separator comprisingia rotatable drum, feeding means deliveringito the .lowerend thereo.f,xa central and a .peri-ph eral discharge at the top of said drum, an in dependently rotatable screw, and spiral shares cooperating with said screw and delivering the lighter articles to said central discharge and the eavier particles to the peripheral discharge.
  • a centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a central and a peripheral discharge at the top of said drum, an independentlyrotatable screw, and spiral shares cooperating with said screw and delivering the lighter particles to said central discharge and the heavier particles to the peripheral discharge, and a partition dividing said shares.
  • a centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a central and a peripheral discharge at the top of said drum, an independently-rotatable screw, and means cooperating with said screw for delivering the lighter and heavier particles respectively to "aid central and peripheral discharge.
  • a centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a discharge at the top, an independently-rotatable screw, a spiral share cooperating with said screw and detoo livering to said discharge, and a plurality of fingers carried by said screw and engaging saidrdrum.
  • a centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a central and a periph eral discharge at the top of said drum, an independently-rotatable screw, spiral shares cooperating with said screw and delivering the li hter particles to said central discharge and t e heavier articles to the peripheral discharge, and a plhrality of fingers carried by said screw.
  • a centrifugal separator including a screw and a double discharge, and a spiral share delivering to each discharge, one share being located relatively near the aXis of said screw and the other near the periphery thereof.
  • a centrifugal separator the combination of a stationary feed-pipe, a rotary drum, a screw movable independently of the drum, means for controlling the thickness of the layers of the material to be separated, means for imparting to the material to be treated besides a rotary and transporting motion, a motion influencing the relative position'of the particles of the material, and means for discharging the separated materials at different determined heights and at a determined distance from the center.
  • a centrifugal separator the combination of a stationary feed-pipe, a rotary drum, a screw movable independently of the drum, means for discharging the separated materials at different determined heights and at a determined distance from the center and for keeping back bodies necessary for the separation.
  • centrifugal separators the combination of a stationary feed-tube, a rotary drum, a screw movable independently of the drum, means for controlling the thickness of the layers of the material to be separated, means for imparting to the material to be treated, besides the rotary and transporting motion a motion influencing the relative position of the different particles, and means for discharging the separated materials at a determined distance from the center, ,as described.
  • a centrifugal separator the combination of a device for feeding uniformly the material to be separated, a stationary feedpipe, a conical rotary drum tapering in the direction wherein the solid material is carried, a screw movable independently of the drum, means for controlling the thickness of the layers of the material to be treated, means for imparting to the material to be treated, besides the rotary and transporting motion a motion influencing the relative position of the different particles, and discharging devices for liquid parts at the wider and for solid parts at the narrow part of the drum, as described.

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  • Centrifugal Separators (AREA)

Description

PATENTED OCT. 2, 1906.
W. HOLZER. OENTRIPUGAL SEPARATOR.
APPLICATION FILED JULY 7, 1905.
75)? away UNITED STATES PATENT OFFICE.
CENTRIFUGAL SEPARATOR.
Specification of Letters Patent.
Patented Oct. 2, 1906.
Application filed uly 7,1905- Serial No. 268,705.
To all whom it may concern:
Be it known that I, WILHELM HOLZER, a subject of the German Emperor, and a resident of Nieder-Ramstadt, near Darmstadt, Germany, have invented certain new and useful Improvements in Centrifugal Separators, of which the following is a specification.
This invention relates to a device for separating mixtures of bodies in a continuous manner and with the aid of the centrifugal force.
This device may be used for mixtures of difl'erent composition,as well as for different kinds of separation. Thus solid bodies. of different natures contained in a mixture may be separated one from the other. In the same manner solid or muddy parts may be separated from a mixture composed chiefly of liquid. Furthermore, liquids adhering to solid bodies may be separated from the latter.
In the annexed drawings, Figure 1 is a section of the device, some of the internal parts being shown in side elevation. Fig. 2 is a section on line a b of Fig. 1. Fig. 3 shows a section on line 7c Z of the same figure. Fig. 4 shows a modification of the device shown in Fig. 1, this figure being a section on lines f g h i of Fig. 5. Fig. 5 shows a section on line 0 b of Fig. 4.
Similar reference-numerals designate like parts throughout all the figures. I
3 is a pipe fixed outside the centrifugal apparatus in any suitable manner and projecting into the latter as a completely stationary pipe which is in no direct connection with the apparatus.
5 is a conical mantle mounted on the shaft 6, round which it can rotate. This mantle is held at the desired height in any preferred appropriate manner. This shaft 6 is rotatably supported in its lower part (not shown) and carries fixed upon it the screw 4, as well as the parts secured to the latter- The screw 4 leaves near its axis a hollow space or core through which the stationary pipe 3 projects in the centrifugal apparatus. Alongside the inner opening of the screw 4 stiffening webs or stays 2.5 are provided, which are rigidly secured to the screw 4 or cast in one piece with the latter. These stiffening-stays are arranged round the inner opening of the screw 4, as shown by Fig. 3. They are only shown on both sides in Figs. 1 and 4 for sake of clearness. Besides this the height of pitch of the screw 4 diminishes toward the top. Between the turns of the screw 4 are rakes 15, connected to the screw 4 by means of the bolts 24, round which they can rotate, while their free ends slide along the inner periphery 'of the centrifugal mantle.- As
best shown by Fig. 3, these rakes also exist in a certain number, only two rakes being shown in Fig. 1 on both sides of the worm 1n order to not complicate the drawings. The screw 4 carries at its upper end, either rigidly secured to it or cast integral with it, first a spirally-wound share 16, then above this a circular plate 22, and above the latter a second spirally-wound share 18. Plate 22 produces separate chambers for the shares 16 and 18. The top of the mantle 5 is closed by a cover which is provided with a funnelshaped opening 17 and an annular opening 19 surrounding the latter. The funnel may as well be made of one piece with the screw 4 and project through the cover of the cen-- trifugal separator. The part of the share 16 which is nearer to the center is directed obliquely upwardly and forms the continuation of the opening 17, and the said centralpart of this opening is a part of the said opening, while the share 18 continues in the same manner the opening 19. Both the shares, as well as the screw 4, to which they are rigidly connected, can rotate freely with regard to the mantle of the centrifugal separator and the upper parts of it.
In the lower part of the mantle 5 the latter is tightly connected to the shaft 6 by means of a stuff ing-box 25. Besides this the separating apparatus above described is connected with a device (not shown in the drawings) which delivers in a continuous and uniform manner to the pipe 3 the mixture to be treated.
According to the nature of the material to be treated several modifications can be made in the device above described. Fig. 4 shows a narrower screw 4 and only one share 18*, another modification consisting in that the discharge-channels 17 a are rigidly connected to the screw 4 or made integral with the latter. Furthermore, these discharge-channels 19 are arranged on the same area of a circle and form a sort of cell upon the latter. In this instance the interval between the cellular channels 17 a and the-cover 0r mantle of the The exhaust-openings are arranged at different heights.
centrifugalseparatoris closed by the ring 26, which is connected to the cells 17' in such a manner that it follows their rotary motion, while being adapted to be freely moved downwardly and upwardly. In-the form shown by Fig. 4 the discharge-channels 17 are cylindrical. However, they may also be conical when the nature of the material to be treated requires it. The same remarks may be made on behalf of the connecting-pieces of the shares. Furthermore, according to the nature of the material and the properties which the final productmust have, the rakes 15'ma'y be dispensed with; also the mantle 5, according to the nature of the material and the-requirements, may be perforated or not. The mantle 5, as well as the shaft 6, is pro vided with a drivingdevice which may have the most'varying forms and which for this reason is not shown inthe drawings.
The function of thedevice is as follows: Assuming that a mixture is to be treated which is composed of different kinds of solid bodies which are to be separatedone from the other, the mixture introduced by the charging device (not shown) falls through the tube 3 uniformly on the bottom of the rotating centrifugal apparatus, where it is thrown againstthe wall of the latter by reason of the centrifugal force: As the pipe 3 does not rotate, th'ere is no danger of the mixture adhering 'to-the wall of the tube. The screw 4 ro tates in the same direction as the mantle 5 of the centrifugal apparatus, but with a different speed. According to the sense of the worm 4with reference to the direction of rotationof the whole, the motion of the screw 4 ismore rapid or less rapid than the motion of the centrifugal "apparatus. It results from this difference'of speed between the centrifugal apparatus 5 and the screw 4 a raising motionof therniXed material which forms an annular couchalong the periphery of the separator. During its ascensional motion of the mixed material it is'continuously loosened and liftedoff the periphery, so that the heavier particles-can arrive n'ear the periphery and-push the'lighter particles more toward the center. In this manner :thebodies of the same kind will during their raising motion accumulate in annular 'COL1Ch6S,"tl16 lighter bodies-lying nearer to the center, while. the
heavier-ones are adjacent to theperiphery. ln ord'er to facilitate the separation, a little quantity of'watermay be added tothelmixture; and this 'water i. 'e., the part-of it which has not-penetrated into the couches of material forms a :further couch near the center; The water is prevented from escaping by-the cover of the apparatus, and it can onlyescapethrough the opening situated nearest to lthe periphery, and its escape is exactly regulated upon the quantity of fresh. Water introduced. It is impossible that the water huddles in an inconvenient manner the material treated. WVhen the latter has arrived at the top of the apparatus in separated annular couches, the couch which is nearest to the center is pushed toward the center by the share .16 and brought in the way of the discharge-opening 17, through which this couch escapes on the inclined plane of the share 16 and the discharge-channel toward the top and the outside. Here it is collected and carried away in any convenient manner. The heavier couch does not come in the way of the share 16 and is brought by the prolongationof the screw 4 farther to; ward the top in the way of the share 18, which brings it into the ,-discharge.- opening,19, whence it escapes on the inclined plane, of the share upward and outward over the cover of the centrifugal separator in order to be collected and carried away in turn in any convenient manner. It is very important, that the escape of the different materials takes place at different heights, so that different kinds of material can be separately collected and carried away at these'different heights. The pitch of the worm 4 diminishes toward the top in order to preventthe thicknessof the ring of material decreasing by reason of the increase of the diameter of the separator A considerable decrease of the ring of material would have an unfavorableinfluence on;the separating operation. In fact, the formation of couches would easily be more or less destroyed. a The guidance of theseparated material before the discharging toward the center, and consequently the mounting;,of acover, has-been necessary,ias it has already been stated, for keeping the Water in the centrifu gal apparatus. Anotherobject of thatarrangement is that the material which near the center escapes witha lesser speed is less exposed to destruction when strikingthe;co1 lecting apparatus. Consequently the whole apparatus requires, less mechanical work, as the inertia of the bodies escaping with a little speed is lesser. 1. 1
Besides the separation of .two, different materials a greater number ,of different kinds of materials may be discharged within certain practical limits. In, this case a CQIIGgspondingly-greaternumber of shares and discharge openings are arranged. i i
The mantleof the centrifugal apparatus is enlarged at the top in orderto facilitatethe raising motion of the material. However, the. enlargement of the mantle must only be sufficient to keep the upward motion .of the material in dependence of the relative motion of.the-sc.rew4.. I J According tothe nature of the material vto be treated the process is somewhatmodiiied. Thus when a miXtureis treated whichis essentially composed of liquidandfrom which solid ormuddyparts are to s separated the above-described loosening of the mixture is not necessary, so that the rake 15 may be dispensed with. Furthermore, one of the shares may be omitted, as the liquid escapes quite automatically in proportion as fresh liquid is introduced through the tube 3. is, however, necessary to put the escape of the solidor muddy parts as near to the center as the escape of the liquid, as otherwise the latter would escape through the opening provided for the muddy parts and would again be mixed with the latter. In order to prevent this, the form of cells shown in Figs. 4 and 5 has been given to the escape-openings. If, on the contrary, a material substantially composed of solid bodies is to be separated from the adherent liquid, this may be carried out intwo ways by the above-described construction. The mantle of the apparatus may receive the form of a sieve and a less-importtant number of rakes may be made to slide along the periphery in order to keep the holes of the sieve open and the mass loose. The liquid may thus escape freely. Another possibility is to leave the mantle without holes, but to render it smaller at the top. The liquid to :be separated is first projected against the periphery of the centrifugal apparatus, while the solid material is raised by the screw. The liquid, partly by gravitation, partly by the influence of the centrifugal force, flows downwardly in the material loosened and kept permeable by the rakes along the wall inclined obliquely downward and outward. The liquid escapes at the lower end through special openings. It is particularly important that inthis case the mantle of the separator is larger at the base than at the top, as the centrifugal force drives the liquid toward the larger end, while in the opposite case it would be driven to the spot where the solid bodies should have the greatest degree of dryness, which would be contrary to the object viewed. In the arrangement described the liquid encounters on its way toward the outside only material which is moister and moister. In both cases only one share would be necessary at the upper mouth and one escape-opening, if -it is not desired to effect simultaneously with the separation of the liquid a special separation of the solid bodies between them.
Having now fully described my said in vention, what I claim, and desire to secure by Letters Patent, is
1. A centrifugal separator comprising a stationary feed-pipe, a rotatable conical drum provided with discharge-openings, a screw rotatable independently of the drum, and a plurality of fingers projecting outwardly from opposite sides of the blades of said screw to the drums.
2. A centrifugal separator comprising a stationary feed-pipe, a rotatable conical drum provided with centrally-disposed discharge-openings, a screw rotatable independently of the drumand provided with blades .drum provided with centrally-disposed :dis-
charge-openings, a screw rotatablezindependently of the drum, ,and .a pluralityof radially-disposed fingers secured to .and projecting from opposite sides of the blades of said screw, theouter ends of said fingers engaging the inner periphery of the drum.
4. A centrifugal separator comprising a stationary feed-pipe, a rotatable conical drum, a screw'rotatable independentlyofathe drum, a plurality of fingers projecting radially from the blades of said screw,:and spiral shares 16 and 18 cooperating with theidelivery end of said screw.
5. A centrifugal separatorcomprisinga rotatable drum, feeding means delivering to the lower end of said-drumand aidischargeiat the upper end thereof, an independently-rotatable screw, and a share cooperating with said screw anddelivering to saiddischarge.
6. A centrifugalseparatorcomprisingarotatable drum, feeding means delivering to the lower end of said drum and a-disc'harge at the upper end thereof, an independently-rotatable screw, and a spiral share cooperating with said screw and delivering to said discharge.
7. A centrifugal separator comprisingia rotatable drum, feeding means deliveringito the .lowerend thereo.f,xa central and a .peri-ph eral discharge at the top of said drum, an in dependently rotatable screw, and spiral shares cooperating with said screw and delivering the lighter articles to said central discharge and the eavier particles to the peripheral discharge.
8. A centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a central and a peripheral discharge at the top of said drum, an independentlyrotatable screw, and spiral shares cooperating with said screw and delivering the lighter particles to said central discharge and the heavier particles to the peripheral discharge, and a partition dividing said shares.
9. A centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a central and a peripheral discharge at the top of said drum, an independently-rotatable screw, and means cooperating with said screw for delivering the lighter and heavier particles respectively to "aid central and peripheral discharge.
10. A centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a discharge at the top, an independently-rotatable screw, a spiral share cooperating with said screw and detoo livering to said discharge, and a plurality of fingers carried by said screw and engaging saidrdrum. v
11. A centrifugal separator comprising a rotatable drum, feeding means delivering to the lower end thereof, a central and a periph eral discharge at the top of said drum, an independently-rotatable screw, spiral shares cooperating with said screw and delivering the li hter particles to said central discharge and t e heavier articles to the peripheral discharge, and a plhrality of fingers carried by said screw.
12. A centrifugal separator including a screw and a double discharge, and a spiral share delivering to each discharge, one share being located relatively near the aXis of said screw and the other near the periphery thereof.
13. In a centrifugal separator the combination of a stationary feed-pipe, a rotary drum, a screw movable independently of the drum, means for controlling the thickness of the layers of the material to be separated, means for imparting to the material to be treated besides a rotary and transporting motion, a motion influencing the relative position'of the particles of the material, and means for discharging the separated materials at different determined heights and at a determined distance from the center.
14. In a centrifugal separator the combination of a stationary feed-pipe, a rotary drum, a screw movable independently of the drum, means for discharging the separated materials at different determined heights and at a determined distance from the center and for keeping back bodies necessary for the separation.
15. In centrifugal separators the combination of a stationary feed-tube, a rotary drum, a screw movable independently of the drum, means for controlling the thickness of the layers of the material to be separated, means for imparting to the material to be treated, besides the rotary and transporting motion a motion influencing the relative position of the different particles, and means for discharging the separated materials at a determined distance from the center, ,as described.
16. In a centrifugal separator the combination of a device for feeding uniformly the material to be separated, a stationary feedpipe, a conical rotary drum tapering in the direction wherein the solid material is carried, a screw movable independently of the drum, means for controlling the thickness of the layers of the material to be treated, means for imparting to the material to be treated, besides the rotary and transporting motion a motion influencing the relative position of the different particles, and discharging devices for liquid parts at the wider and for solid parts at the narrow part of the drum, as described.
In testimony whereof I have hereunto set my hand in presence of two Witnesses.
WILHELM HOLZER. Witnesses:
JEAN .GRUND,
CARL GRUND.
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US2614748A (en) * 1947-07-29 1952-10-21 Howard P Ritsch Centrifuge for separating solids
US2743864A (en) * 1954-03-05 1956-05-01 Bird Machine Co Centrifuge with inclined conveyor blade and vanes for rapid collection of fine particles from suspensions
US2862658A (en) * 1952-05-28 1958-12-02 Separator Ab Method and apparatus for centrifugal separation of a mixture of solids and two liquids
US5261869A (en) * 1992-04-06 1993-11-16 Alfa Laval Separation, Inc. Decanter centrifuge having discontinuous flights in the beach area
US5509882A (en) * 1994-09-12 1996-04-23 Tetra Laval Holdings & Finance S.A. Decanter centrifuge having an offset conveyor flight to aid rinsing
US5653673A (en) * 1994-06-27 1997-08-05 Amoco Corporation Wash conduit configuration in a centrifuge apparatus and uses thereof
US20020132718A1 (en) * 2000-08-31 2002-09-19 Koch Richard James Centrifuge for separating fluid components
US20030096691A1 (en) * 2000-08-31 2003-05-22 Koch Richard James Centrifuge systems and methods
US6572524B1 (en) 2000-07-14 2003-06-03 Alfa Laval Inc. Decanter centrifuge having a heavy phase solids baffle
US6605029B1 (en) * 2000-08-31 2003-08-12 Tuboscope I/P, Inc. Centrifuge with open conveyor and methods of use
US20030228966A1 (en) * 2000-08-31 2003-12-11 Koch Richard James Centrifuge systems and methods
US9597618B2 (en) 2009-11-05 2017-03-21 Daritech, Inc. Systems and methods for extracting sand from raw slurry material
US9610521B2 (en) 2009-11-05 2017-04-04 Daritech, Inc. Systems and methods for extracting particulate from raw slurry material
US10286340B2 (en) 2014-05-27 2019-05-14 Daritech, Inc. Feed systems and methods for rotary screen separators
US10603611B2 (en) 2014-05-30 2020-03-31 Daritech, Inc. Cleaning systems and methods for rotary screen separators
US10603675B2 (en) 2014-11-02 2020-03-31 Dari-Tech, Inc. Systems and methods for extracting particulate from raw slurry material
EP2478762B1 (en) * 2011-01-20 2023-06-07 Daritech, Inc. Systems and methods for extracting particulate from raw slurry material

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