US2559917A - Centrifuge bowl with reciprocating valve for discharging solids from the bowl - Google Patents

Centrifuge bowl with reciprocating valve for discharging solids from the bowl Download PDF

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US2559917A
US2559917A US636779A US63677945A US2559917A US 2559917 A US2559917 A US 2559917A US 636779 A US636779 A US 636779A US 63677945 A US63677945 A US 63677945A US 2559917 A US2559917 A US 2559917A
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solids
piston
centrifuge
bowl
discharge
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Paul J Gresham
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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
    • B04B1/10Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
    • B04B1/14Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge

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  • This invention relates to the separation of solids from liquids, and is of particular utility for handling a large volume of solids-in-liquid infiuent, such for example as encountered in sewage disposal, and effectively separating the solids from the liquid thereof.
  • the primary object of the invention is to provide improved means for removing, from within the centrifuge chamber, solids which are progressively segregated and accumulated under the action of centrifugal force exerted during the normal operation of the centrifuge.
  • Another object is to provide a piston type of mechanism adapted to be actuated at intervals to effect expulsion of accumulated solids from within the centrifuge chamber.
  • Still another object is to provide means normally closing the outlet port for solids, but op erable upon movement of the discharge piston to open such port.
  • Another and more specific object is to provide a centrifuge chamber having solids receiving pockets on its inner periphery, and a passage transversely thereof together with a piston movable within such passage to remove accumulated solids from within the passage.
  • a still further object is to provide a discharge passage and a piston cooperating therewith, such elements being so constructed and arranged that solids only are discharged when the piston is actuated.
  • the invention also comprehends the use of piston actuatin means operable at predetermined intervals for moving a plurality of pistons to exhaust solids peripherally of the device.
  • Fig. l is'a vertical sectional view through one form of the device embodying the invention.
  • Fig. 2 is an enlarged detail in section through one of the discharge assemblies
  • Fig. 3 is a detail view of a portion of the pocketed annulus forming an element of the invention
  • Fig. 4 is a detail view in section showing a modified form of the solids discharge mechanism
  • Fig. 7 is a sectional view taken one line 1-1 in Fig. 1.
  • FIG. 1 One form of the invention is shown in Fig. 1 as a centrifuge I comprising a discharge assembly 2 secured to conical housing members 3 and s to which the shafts 5 and 6 are attached, the
  • the shaft 5 is tubular to provide an inlet to the interior of the centrifuge I as will be more fully described.
  • a suitable source of power (not shown) is operably connected to one of the shafts 5 or 6 to impart adequate rotational speed to the centrifuge to effect centrifugal separation of the solids from the liquids of the influent introduced to the chamber within the housing I.
  • a scraper blade l2 extends transversely of the ring ll proximate its lowermost portion and serves to remove the solids from upon the inner periphery of the member II.
  • the discharge assembly 2 includesthe annulus l5 to which are attached the peripheral edges of the conical members 3 and 4 of the housing I. The opposite ends of these members are in turn secured to the shafts 5 and 6.
  • a hollow body It of a symmetrical configuration and complementary with the interior of the housing I.
  • a plurality of parallel conical guiding walls shown at I! and i8 there being a plurality of spacer fins or vanes l9 interposed and secured to the successive members so that there are provided a plurality of radially extendingpassages Z8, 2! and 22.
  • This construction requires that the fluids introduced to the device move radially thereof while spread into thin sheets, and the fins IS in the respective passages prevent peripheral slip between the centrifuge and the material passing therethrough. The structure therefore enhances the application of centrifugal force to effect desired separation of the solids from the liquids of the influent introduced through the shaft 5.
  • the inner periphery of the annulus E has oppositely tapering surfaces and 25 (Fig. 3) which terminate at their outermost ends in cylindrical pockets 21 which, as clearly shown in Fig. 2, are in alignment with the bore of the transverse cylinder 35 which has its opposite ends extending sidewardly from the annulus.
  • of the cylinder comprises the discharge port It! and has provided thereon a support member 32 with the car 33 thereon for a pivotal connection 34 with the valve or closure member 35 engageable with the outer end as of the cylinder to form a closure therefor.
  • the pivot 34 is located radially inward of the port It and hence the valve 35 tends to remain normally closed from centrifugal force exerted thereon.
  • the opposite end 40 of the cylinder 30 has a piston 4
  • a seal ring 42 of a suitable type forms a seal with the inner Wall of the cylinder 38 whereby leakage of fluids past the piston is prevented.
  • shall be moved axially of the cylinder 30 toward the discharge port i0. Such movement causes the inner end of the piston to traverse the respective pockets 2? in the annulus I5 and hence any solids collected in a given pocket and the adjacent discharge port will be moved by the piston into a compact mass within the port. Continued'movement of the piston 4
  • in the discharge assembly 2 may be operated in any desired sequence, or simultaneously. In any event operation should be such as to minimize the possibility of creating a condition of eccentricity within the centrifuge.
  • a spider 5G is attached to the pistons 4
  • a pneumatically or hydraulically actuated mechanism generally referred to as 54, and comprising a stationary annular cylinder 55 having an annular piston 56 therein.
  • This piston is attached through studs 5'? to a disk 58, there being a thrust bearing 59 interposed between such disk and the thrust ring 5
  • the thrust bearing 65 Interposed between the base of the cylinder 55 and a collar 35: on the shaft E, is the thrust bearing 65, it being apparent that the bearings 58 and Si permit the assembly 54 to remain stationary while the remainder of the device is r0- tated.
  • Pressure fluid is admitted to the cylinder 55 and beneath the piston 55 through the pipe 5.2 connected to a suitable source of pressure fluid. It is to be understood that the actuation of this echanism can be effected at any desired sequence of intervals either manually or automatically.
  • FIG. 4 A modified form of the discharge assembly is shown in Fig. 4 and like parts thereof are identified by like reference characters.
  • is provided with a continuation 70 having an enlarged bore ll within which the differential piston "12 is movable.
  • This piston has an inner face 73 which is of smaller areal extent than the outer face 74, it being intended that the piston shall normally assume the position indicated in the drawings whereby the discharge port I0 is maintained closed. Fluid pressure is exerted upon the face 14 through the connection 15 of which the passage 16 communicates through the opening 18 to the interior of the chamber I.
  • centrifugal force acting upon the face It is greater than the force acting upon the face 73 whereby the valve is normally maintained in closed position.
  • the piston 41' in this form of the invention is shown as having a clearance at 99 to permit extrusion of liquid or semi-liquid from within the passage before the valve 12 opens, alternately of course, the stepped piston 4
  • toward the differential piston 12 will impact accumulated solids which will in turn force the piston l2 outwardly or to the right so that such solids will move under centrifugal force to and through the discharge port
  • the embodiment shown in Fig. 5 is similar to that just described, but the centrifugal force of fluid acting upon the face 74 of the piston 12 is supplemented by the compression spring which is interposed between the piston and the outer end of the passage within which the piston moves.
  • has a stem 89 thereon. This stem is attached to the piston 8! which forms a closure for the discharge port I9".
  • the piston assembly moves inwardly, accumulated solids are moved therewith and such solids are thrown outwardly by centrifugal force and through the discharge port I0" when such port is uncovered by movement of the assembly.
  • the inner end of the piston t! enters the bore 82 so that a closure is formed to prevent the leakage of fluid during the interval of discharge of solids from the port 10''.
  • the invention comprehends new and useful improvements in a centrifuge, and particularly mechanisms for removing solids from within the centrifuge chamber during continued operation thereof whereby the solids are effectively removed from a solids-in-liquid influent.
  • a centrifugal separator comprising a centrifuge chamber having peripheral intersecting whereby the solids are impacted therebetween,
  • closure means opened to exhaust solids from within the passage.
  • a centrifugal separator comprising, a centrifuge body having intersecting radial and transverse passages in its periphery for the discharge of solids accumulated in the transverse passage, a piston in one end of said passage, there being a discharge port in the other end of the passage, closure means movable under centrifugal force to normally close said discharge port, a stepped end on said piston to enter the passage to entrap solids proximate said closure means and to thereafter open said means and discharge the entrapped solids, said stepped portion being of a length that the larger portion of the piston closes the radial passage as the end of the piston approaches the closure means.
  • a centrifugal separator comprising a chamber having a radial passage and a transverse passage at the outer end thereof forming a passage between the interior and the exterior of the chamber, means normally closing one end of the transverse passage, a stepped piston in the transverse passage opposite said means, and means for moving the piston toward said closure to impact solids within the transverse passage and to thereafter close the passage inwardly of the outer end and then move the closure means to open position whereby the impacted solids are exhausted from the passage.

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  • Centrifugal Separators (AREA)

Description

July 10, 1951 P. J. GRESHAM 2,559,917
CENTRIFUGE BOWL WITH RECIPROCATING VALVE I FOR DISLHARGING SOLIDS FROM THE BOWL Filed Dec. 22, 1945 3 Sheets-Sheet l l'[ (D |I 1 (Q o I 3 9 gW/ag S 5 t) m .I
Bil/L J. GRESHAM INVENTOR BY aw @fM July 10, 1951 P. J. GRESHAM 2,559,917
. CENTRIFUGE BOWL WITH RECIPROCATING VALVE FOR DISCHARGING SOLIDS FROM THE BOWL 5 Sheets-Sheet 2 Filed Dec. 22, 1945 INVENTOR. M4 M PAUL J. GRESHAM .5 5 m 0 T T A July 10, 1951 P. J. GRESHAM 2,559,917
CENTRIFUGE BOWL WITH RECIPROCATING VALVE FOR DISCHARGING SOLIDS FROM THE BOWL 3 Sheets-Sheet 3 Filed Dec. 22, 1945 5401. J. GEES HAM A HORNE YS Patented July 10, 1951 UNITED STATES PTENT OFFICE CENTRIFUGE BOWL WITH RECIPROCATIN G VALVE FOR DISCHARGING SOLIDS FROM THE BOWL 3 Claims.
This invention relates to the separation of solids from liquids, and is of particular utility for handling a large volume of solids-in-liquid infiuent, such for example as encountered in sewage disposal, and effectively separating the solids from the liquid thereof.
The invention relates and broadly comprehends the subject matter of my co-pending application, Serial Number 593,274, filed May 11, 1945, now abandoned, and constitutes an improvement of the invention disclosed therein.
The primary object of the invention is to provide improved means for removing, from within the centrifuge chamber, solids which are progressively segregated and accumulated under the action of centrifugal force exerted during the normal operation of the centrifuge.
Another object is to provide a piston type of mechanism adapted to be actuated at intervals to effect expulsion of accumulated solids from within the centrifuge chamber.
Still another object is to provide means normally closing the outlet port for solids, but op erable upon movement of the discharge piston to open such port.
Another and more specific object is to provide a centrifuge chamber having solids receiving pockets on its inner periphery, and a passage transversely thereof together with a piston movable within such passage to remove accumulated solids from within the passage.
A still further object is to provide a discharge passage and a piston cooperating therewith, such elements being so constructed and arranged that solids only are discharged when the piston is actuated.
The invention also comprehends the use of piston actuatin means operable at predetermined intervals for moving a plurality of pistons to exhaust solids peripherally of the device.
The foregoing objects are primary objects, which, together with other objects and advantages of the invention, will be more fully apparent from the following description considered in connection with the accompanying drawings in which:
Fig. l is'a vertical sectional view through one form of the device embodying the invention;
Fig. 2 is an enlarged detail in section through one of the discharge assemblies;
Fig. 3 is a detail view of a portion of the pocketed annulus forming an element of the invention;
Fig. 4 is a detail view in section showing a modified form of the solids discharge mechanism,
charge assembly which includes synchronously movable pistons for moving segregated solids to the discharge port;
Fig. 7 is a sectional view taken one line 1-1 in Fig. 1.
One form of the invention is shown in Fig. 1 as a centrifuge I comprising a discharge assembly 2 secured to conical housing members 3 and s to which the shafts 5 and 6 are attached, the
entire centrifuge being mounted upon bearings l and 8. The shaft 5 is tubular to provide an inlet to the interior of the centrifuge I as will be more fully described. A suitable source of power (not shown) is operably connected to one of the shafts 5 or 6 to impart adequate rotational speed to the centrifuge to effect centrifugal separation of the solids from the liquids of the influent introduced to the chamber within the housing I.
It is intended that segregated solids will be discharged from the ports 10 of the assembly 2, during rotation of the centrifuge and in a manner to be more fully described, and that such solids will be thrown by centrifugalforce outwardly against the collector ring H which is rotated slowly by means of asuitable source of power (not shown). A scraper blade l2 extends transversely of the ring ll proximate its lowermost portion and serves to remove the solids from upon the inner periphery of the member II.
The discharge assembly 2 includesthe annulus l5 to which are attached the peripheral edges of the conical members 3 and 4 of the housing I. The opposite ends of these members are in turn secured to the shafts 5 and 6.
Interiorly of the chamber, formed by the elements to which reference has justbeen made, is a hollow body It of a symmetrical configuration and complementary with the interior of the housing I. Interposed between such body and the outer wall of the centrifuge are a plurality of parallel conical guiding walls shown at I! and i8, there being a plurality of spacer fins or vanes l9 interposed and secured to the successive members so that there are provided a plurality of radially extendingpassages Z8, 2! and 22. This construction requires that the fluids introduced to the device move radially thereof while spread into thin sheets, and the fins IS in the respective passages prevent peripheral slip between the centrifuge and the material passing therethrough. The structure therefore enhances the application of centrifugal force to effect desired separation of the solids from the liquids of the influent introduced through the shaft 5.
The inner periphery of the annulus E has oppositely tapering surfaces and 25 (Fig. 3) which terminate at their outermost ends in cylindrical pockets 21 which, as clearly shown in Fig. 2, are in alignment with the bore of the transverse cylinder 35 which has its opposite ends extending sidewardly from the annulus. The end 3| of the cylinder comprises the discharge port It! and has provided thereon a support member 32 with the car 33 thereon for a pivotal connection 34 with the valve or closure member 35 engageable with the outer end as of the cylinder to form a closure therefor. The pivot 34 is located radially inward of the port It and hence the valve 35 tends to remain normally closed from centrifugal force exerted thereon. To enhance this tendency and hence assure positive closure of the valve 35 upon the seating surface 35, there is provided a stud 36 in the valve member and such stud is provided with a weight 31 thereon. It seems apparent that centrifugal force acting upon the weight 3? greatly increases the force which holds the valve upon its seat, and hence closure of the discharge port i0 is maintained except when discharge of solids therefrom is effected as hereinafter described.
The opposite end 40 of the cylinder 30 has a piston 4| slidably fitting therein. A seal ring 42 of a suitable type forms a seal with the inner Wall of the cylinder 38 whereby leakage of fluids past the piston is prevented.
It is intended, as will more fully appear in the description of the operation of the device of the invention, that each of the pistons 4| shall be moved axially of the cylinder 30 toward the discharge port i0. Such movement causes the inner end of the piston to traverse the respective pockets 2? in the annulus I5 and hence any solids collected in a given pocket and the adjacent discharge port will be moved by the piston into a compact mass within the port. Continued'movement of the piston 4| will cause the valve member 35 to open whereby the extruded solids will discharge radially under centrifugal force to the interior of the ring I for disposition in the manner already explained.
Attention is directed to the fact that the inner end of the piston 4| is reduced in diameter at 43 whereby a shoulder 44 is formed thereon. The reduced portion 43 enters the discharge port H3 with a slight clearance whereby any liquid or semi-liquid within the discharge port will move toward the interior of the centrifuge chamber as the piston advances. On the other hand, the solids are advanced by the piston and will, when sufficient force is applied, open the valve 35 whereby the solids are progressively discharged. The shoulder 44 on the'piston enters the discharge port I!) just before the solids are completely discharged, and in this manner a closure is formed that prevents leakage of liquids past the piston and through the port H! at the instant all solids are removed therefrom under centrifugal force. As the piston moves to terminal position an abutment 45 thereon engages the valve 35 so that all solids are free to move outwardly under centrifugal force while the valve. is held open.
The pistons 4| in the discharge assembly 2 may be operated in any desired sequence, or simultaneously. In any event operation should be such as to minimize the possibility of creating a condition of eccentricity within the centrifuge. Preferably, as shown in Fig. l, a spider 5G is attached to the pistons 4| while the opposite end of such spider is attached to a thrust ring 5i engaged by the compression spring 52 surrounding the shaft 6 and normally urging the spider outwardly to hold the pistons 4| in their outermost position as shown in Figs. 1 and 2.
It seems apparent that when the spider 58 is moved against the tension of the spring 52, as indicated by the arrow 53, discharge of solids from the respective cylinders 30 is initiated. To effect this movement there is provided a pneumatically or hydraulically actuated mechanism generally referred to as 54, and comprising a stationary annular cylinder 55 having an annular piston 56 therein. This piston is attached through studs 5'? to a disk 58, there being a thrust bearing 59 interposed between such disk and the thrust ring 5|.
Interposed between the base of the cylinder 55 and a collar 35: on the shaft E, is the thrust bearing 65, it being apparent that the bearings 58 and Si permit the assembly 54 to remain stationary while the remainder of the device is r0- tated.
Pressure fluid is admitted to the cylinder 55 and beneath the piston 55 through the pipe 5.2 connected to a suitable source of pressure fluid. It is to be understood that the actuation of this echanism can be effected at any desired sequence of intervals either manually or automatically.
The operation of the device is believed apparent from the foregoing description of an illustrative embodiment of the invention. By way of summary and supplementation, it will be as sumed that all parts are in the relative positions shown in Fig. 1. A solids-in-liquid influent is introduced through the shaft 8 while the entire centrifuge is rotated at a desired speed. The in fluent enters the centrifuge chamber and moves in thin sheets along the plurality of paths defined by the body it, the centrifuge housing the interposed dividing walls i? and i8, and the interconnecting fins i5. Energy is imparted to the moving material as it moves outwardly toward the discharge assembly 2 and at the same time the separation of solids from the liquids takes place progressivel the solids tending to move along the outer surfaces of the respective passages and thence discharging upon the surfaces and 26 of the annulus 65. These solids then move into the pockets 2?.
At intervals the pistons 4! are moved toward the discharge ports iii whereby accumulated solids within the pockets 2'? and the discharge ports are extruded as the respective valves 35 are opened. The solids thus discharged accumulate upon the inner periphery of the ring H which, as already explained, is rotated slowly so that the scraper i2 removes such solids for desired disposition.
While, as above indicated, rotational energy is imparted to the material moving outwardly toward the discharge assembly 2, a major portion of such energy is returned to the rotating system as the fluids move inwardly from the assembly 2 toward the fluids discharge openings 2 proximate the axis of rotation. It is thus apparent that energy losses are confined to friction and windage and the kinetic energy of the solids discharged from the assembly 2 and of the liquids discharged from the openings 24. Suitable collector means for the exhausted liquid (not shown) will of course be provided to conduct the eflluent from the device.
A modified form of the discharge assembly is shown in Fig. 4 and like parts thereof are identified by like reference characters. In this construction, however, the end 3| is provided with a continuation 70 having an enlarged bore ll within which the differential piston "12 is movable. This piston has an inner face 73 which is of smaller areal extent than the outer face 74, it being intended that the piston shall normally assume the position indicated in the drawings whereby the discharge port I0 is maintained closed. Fluid pressure is exerted upon the face 14 through the connection 15 of which the passage 16 communicates through the opening 18 to the interior of the chamber I. By means of this construction, centrifugal force acting upon the face It is greater than the force acting upon the face 73 whereby the valve is normally maintained in closed position.
The piston 41' in this form of the invention is shown as having a clearance at 99 to permit extrusion of liquid or semi-liquid from within the passage before the valve 12 opens, alternately of course, the stepped piston 4| of Fig. 2 may be used. In any event, movement of the piston 4| toward the differential piston 12 will impact accumulated solids which will in turn force the piston l2 outwardly or to the right so that such solids will move under centrifugal force to and through the discharge port The embodiment shown in Fig. 5 is similar to that just described, but the centrifugal force of fluid acting upon the face 74 of the piston 12 is supplemented by the compression spring which is interposed between the piston and the outer end of the passage within which the piston moves.
In the embodiment of Fig. 6 the piston 4| has a stem 89 thereon. This stem is attached to the piston 8! which forms a closure for the discharge port I9". As the piston assembly moves inwardly, accumulated solids are moved therewith and such solids are thrown outwardly by centrifugal force and through the discharge port I0" when such port is uncovered by movement of the assembly. At the same time however, the inner end of the piston t! enters the bore 82 so that a closure is formed to prevent the leakage of fluid during the interval of discharge of solids from the port 10''.
While the foregoing description has referred to specific structures embodying the invention and has referred to the specific use of the device for sewage treatment, it is intended that such references are by way of illustration only and not of limitation.
Broadly the invention comprehends new and useful improvements in a centrifuge, and particularly mechanisms for removing solids from within the centrifuge chamber during continued operation thereof whereby the solids are effectively removed from a solids-in-liquid influent.
The invention claimed is:
1. A centrifugal separator comprising a centrifuge chamber having peripheral intersecting whereby the solids are impacted therebetween,
and the closure means opened to exhaust solids from within the passage.
2. A centrifugal separator comprising, a centrifuge body having intersecting radial and transverse passages in its periphery for the discharge of solids accumulated in the transverse passage, a piston in one end of said passage, there being a discharge port in the other end of the passage, closure means movable under centrifugal force to normally close said discharge port, a stepped end on said piston to enter the passage to entrap solids proximate said closure means and to thereafter open said means and discharge the entrapped solids, said stepped portion being of a length that the larger portion of the piston closes the radial passage as the end of the piston approaches the closure means.
3. A centrifugal separator comprising a chamber having a radial passage and a transverse passage at the outer end thereof forming a passage between the interior and the exterior of the chamber, means normally closing one end of the transverse passage, a stepped piston in the transverse passage opposite said means, and means for moving the piston toward said closure to impact solids within the transverse passage and to thereafter close the passage inwardly of the outer end and then move the closure means to open position whereby the impacted solids are exhausted from the passage.
PAUL J. GRESHAM.
' file of this patent:
UNITED STATES PATENTS Number Name Date 273,037 Decastro et al Feb. 27, 1883 802,473 De Raasloif Oct. 24, 1905 921,371 Dibble May 11, 1909 927,059 Kuchs July 6, 1909 943,083 Kuchs Dec. 14, 1909 1,132,814 Weston et al Mar. 23, 1915 1,257,235 Howell Feb. 19, 1918 1,321,353 Bacon Nov. 11, 1919 1,695,990 Altpeter Dec. 18, 1928 1,699,055 Diercks Jan. 15, 1929 1,737,090 Meyers Nov. 26, 1929 1,895,104 Quiroz Jan. 24, 1933 1,960,435 Dudley May 29, 1934 2,104,162 Macklind. Jan. 4, 1938 2,200,202 Harvey May 7, 1940 2,467,742 Hanno Apr. 19, 1949 FOREIGN PATENTS Number Country Date 22,085 Germany June 27, 1883 13,639 Sweden Mar. 2, 1901 129,573 Great Britain July 17, 1919
US636779A 1945-12-22 1945-12-22 Centrifuge bowl with reciprocating valve for discharging solids from the bowl Expired - Lifetime US2559917A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2893628A (en) * 1954-12-07 1959-07-07 Herman Thomas Anthony Solid bowl centrifuge
US3224173A (en) * 1964-12-31 1965-12-21 Nasa Liquid-gas separation system

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Publication number Priority date Publication date Assignee Title
DE22085C (en) * O. LENZ in Berlin Innovations in centrifugal machines for separating solid bodies from liquid bodies or liquids from liquids of lower specific gravity
US273037A (en) * 1883-02-27 Apparatus foe separating bodies of different
US802473A (en) * 1904-06-06 1905-10-24 Harald De Raasloff Valve-regulator for centrifugal machines.
US921371A (en) * 1907-02-18 1909-05-11 Harvey D Dibble Centrifugal separator.
US927059A (en) * 1909-02-23 1909-07-06 Frederick Laist Ore-classifier.
US943083A (en) * 1909-06-30 1909-12-14 Frederick Laist Centrifugal slime-separator.
US1132814A (en) * 1911-05-09 1915-03-23 David B Weston Centrifugal separator.
US1257235A (en) * 1917-12-13 1918-02-19 William G Howell Centrifugal liquid-purifier.
GB129573A (en) * 1919-01-23 1919-07-17 William Adin Chamberlain Improvements in Oil Separators.
US1321353A (en) * 1919-11-11 bacon
US1695990A (en) * 1926-01-30 1928-12-18 Altpeter Ludwig Centrifuge
US1699055A (en) * 1927-06-06 1929-01-15 Diercks Chris Self-draining cream-separator bowl
US1737090A (en) * 1926-01-19 1929-11-26 Nat Aniline & Chem Co Inc Conveying apparatus
US1895104A (en) * 1929-05-29 1933-01-24 Francisco A Quiroz Apparatus for separation
US1960435A (en) * 1928-06-20 1934-05-29 Texas Co Pulverous material injector
US2104162A (en) * 1935-04-08 1938-01-04 William R Macklind Centrifugal separator
US2200202A (en) * 1936-07-25 1940-05-07 Harvey Cecil Ernest Centrifugal machine for the separation of solid and liquid materials
US2467742A (en) * 1943-07-13 1949-04-19 Laval Separator Co De Centrifugal bowl with reciprocating valve for separating sludgecontaining liquids

Patent Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1321353A (en) * 1919-11-11 bacon
US273037A (en) * 1883-02-27 Apparatus foe separating bodies of different
DE22085C (en) * O. LENZ in Berlin Innovations in centrifugal machines for separating solid bodies from liquid bodies or liquids from liquids of lower specific gravity
US802473A (en) * 1904-06-06 1905-10-24 Harald De Raasloff Valve-regulator for centrifugal machines.
US921371A (en) * 1907-02-18 1909-05-11 Harvey D Dibble Centrifugal separator.
US927059A (en) * 1909-02-23 1909-07-06 Frederick Laist Ore-classifier.
US943083A (en) * 1909-06-30 1909-12-14 Frederick Laist Centrifugal slime-separator.
US1132814A (en) * 1911-05-09 1915-03-23 David B Weston Centrifugal separator.
US1257235A (en) * 1917-12-13 1918-02-19 William G Howell Centrifugal liquid-purifier.
GB129573A (en) * 1919-01-23 1919-07-17 William Adin Chamberlain Improvements in Oil Separators.
US1737090A (en) * 1926-01-19 1929-11-26 Nat Aniline & Chem Co Inc Conveying apparatus
US1695990A (en) * 1926-01-30 1928-12-18 Altpeter Ludwig Centrifuge
US1699055A (en) * 1927-06-06 1929-01-15 Diercks Chris Self-draining cream-separator bowl
US1960435A (en) * 1928-06-20 1934-05-29 Texas Co Pulverous material injector
US1895104A (en) * 1929-05-29 1933-01-24 Francisco A Quiroz Apparatus for separation
US2104162A (en) * 1935-04-08 1938-01-04 William R Macklind Centrifugal separator
US2200202A (en) * 1936-07-25 1940-05-07 Harvey Cecil Ernest Centrifugal machine for the separation of solid and liquid materials
US2467742A (en) * 1943-07-13 1949-04-19 Laval Separator Co De Centrifugal bowl with reciprocating valve for separating sludgecontaining liquids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2893628A (en) * 1954-12-07 1959-07-07 Herman Thomas Anthony Solid bowl centrifuge
US3224173A (en) * 1964-12-31 1965-12-21 Nasa Liquid-gas separation system

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