US2578484A - Self-discharging sludge separator - Google Patents
Self-discharging sludge separator Download PDFInfo
- Publication number
- US2578484A US2578484A US760303A US76030347A US2578484A US 2578484 A US2578484 A US 2578484A US 760303 A US760303 A US 760303A US 76030347 A US76030347 A US 76030347A US 2578484 A US2578484 A US 2578484A
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- United States
- Prior art keywords
- piston
- liquid
- space
- flange
- bowl
- 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
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- 239000010802 sludge Substances 0.000 title description 12
- 238000007599 discharging Methods 0.000 title description 3
- 239000007788 liquid Substances 0.000 description 30
- 208000028659 discharge Diseases 0.000 description 19
- 239000012530 fluid Substances 0.000 description 15
- 239000007787 solid Substances 0.000 description 7
- 230000002093 peripheral effect Effects 0.000 description 5
- 230000000717 retained effect Effects 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000011343 solid material Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- MJBPUQUGJNAPAZ-AWEZNQCLSA-N butin Chemical compound C1([C@@H]2CC(=O)C3=CC=C(C=C3O2)O)=CC=C(O)C(O)=C1 MJBPUQUGJNAPAZ-AWEZNQCLSA-N 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 230000002706 hydrostatic effect Effects 0.000 description 2
- MJBPUQUGJNAPAZ-UHFFFAOYSA-N Butine Natural products O1C2=CC(O)=CC=C2C(=O)CC1C1=CC=C(O)C(O)=C1 MJBPUQUGJNAPAZ-UHFFFAOYSA-N 0.000 description 1
- 241001052209 Cylinder Species 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- XXPDBLUZJRXNNZ-UHFFFAOYSA-N promethazine hydrochloride Chemical compound Cl.C1=CC=C2N(CC(C)N(C)C)C3=CC=CC=C3SC2=C1 XXPDBLUZJRXNNZ-UHFFFAOYSA-N 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
Images
Classifications
-
- 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
- B04B1/10—Centrifuges 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
- B04B1/14—Centrifuges 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
- B04B1/16—Centrifuges 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 with discharging outlets controlled by the rotational speed of the bowl
- B04B1/18—Centrifuges 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 with discharging outlets controlled by the rotational speed of the bowl controlled by the centrifugal force of an auxiliary liquid
Definitions
- the present invention relates to a self-discharging sludge separator designed to separate sludge from one or two liquids.
- the invention relates to centrifugal separators of the type in which the bowl is divided into two parts which are adapted to'undergo a relative axial movement at periodic intervals, to aiiord provision for discharge of sludge between the bowlpar ts.
- Such separators are described in my prior Patent No. 2,091,329.
- the slot, or the slots, at the periphery of the bowl, and through which the sludge is discharged are opened and kept in their fully opened condition for a period sufficiently long to permit all the sludge to be discharged.
- the aim of the present invention is to provide means for attaining such a desired opening of the said slot or slots.
- This arrangement ensures that coarse and tough sludge which otherwise will adhere to the sides of the separating drum is given a sufficient opening "of the slot, and sufficiently long time to be discharged from the bowl with as little resistance as possible.
- separators of the type in question it has been aimed to achieve a rapid opening or the peripheral slots by means "of a fluid and rapidly operating valves, but as the time of actual discharge is very short, certain diificulties have been experienced to open the slots to their full extent, because pressure within the separator bowl is decreased during the opening.
- the present invention tends not only to provide a rapid opening of the peripheral slot or slots of the bowl, but likewise to ensure a free or full opening. 'l'his'can be attained by means of an axially disposed reciprocating member for closin said slots provided with an integral- -circular flange between which and a part oi the bowl is arranged a circular groove or space that will hold some of the fluid used for reciprocating the said member.
- the fluid will remain in the circular groove on account of the centrifugal force, and will tend to actuate and force said reciprocating member into open position.
- FIG. 1 shows an axial sectional view of a sludge separator according to the invention
- Fig. 2 is a detail section showing a modification.
- 1 indicates the top part of a separator bowl which in conventional manner is screwedto the bottom parts of the bowl for instance by means of bolts
- a centre tube 2 has attached thereto a discharge ring 3 carrying distributing discs 6, separating plates 5-, and an insert 8 with wings extending into the separator bowl, serving to give the fluid to be treated the same rotationalspeed as the bowl parts.
- the "fluid to be separated is charged through a pipe I into the centre tube 2 from the lower end-of it is conveyed into the actual separating space.
- Thefiirid passes either round the lower end -of the "centre tube and from outside in between the discs 6, or it conveyed through apertures 43- in the lower end of the centre tube 2 upwardly through -distri butin'g holes '32 in the discs 6.
- the lighter components of the fluid will move centripetally between the discs and collect in the space interior to these, "and from here be discharged through the discharge rin 3-, whereas the heavier components of the fluid will pass round the exterior edge or the separa-e ting plates 5 and be discharged through one or several channels or spaces 44 above the said separating plates to the discharge ring '3'.
- the bowl has one or several slots it which are closed durin -separation of the solid components within the bowl by means of a reciprocable annular piston 1'3 mounted in an annular groove the bowl which piston periodically is operated to uncover the slots, thus allowing the sludge col-- lected in the separator bowl to be ejected by centrifugal "force.
- a piston-actuating liquid conveyed to the space or chamber I and subjected to centrifugal force the piston is forced upwardly against a gasket ID to seal the discharge slots II.
- the outer side of the upright portion of the piston I3 may be provided with integrally formed, upper and lower, flexible and resilient lips I2 and I3 which slide on the inner face of the upright cylindrical portion of the lower part I8 and serve as packing rings. Centrifugal force will throw the lips outwardly into sealing position.
- the inner face of the upright portion of the piston may be sealed by a lipped resilient packing ring 28 held in position on the inner part 29 by a suitable retaining ring as shown. These packings I2, Id and 28 are to prevent fluids from by-passing the piston.
- the piston-actuating liquid is sprayed from a tube or tubes 22 into a groove 2I and is by centrifugal force pressed into the bottom of the space or chamber I5 through channels I9.
- a tiny jet of liquid may be constantly sprayed into the groove 2I to provide hydraulic pressure in the space below the piston to ensure the slots I I being held closed during these periods.
- I provide for the quick escape of the liquid beneath the piston so that the pressure within the separator may act on the obtuse edge 3
- I provide one or more relatively large outlets or discharge passages 26, 26 from the bottom of the chamber I5 to the exterior. These passages are controlled by valves 25 which carry pistons 21 and which are of well-known type, being centrifugally operated to closed positions and being hydraulically operated to opened positions.
- the operating liquid When the discharge slots II are to be opened, the operating liquid is sprayed from a tube 23 into a groove 45. By centrifugal force the liquid passes through channels 20 to the spaces at the outer ends of the cylinders in which the pistons 2I reciprocate, the pistons being thus forced inwardly to open the valves 25. The liquid in the space or chamber I5 may then discharge through the passages 26, 26 to release the pressure on the bottom of the piston I3, so that the pressure of the fluid and solid material in the separating section of the body on the edge 3
- the control of the operating liquid may be a four-way valve, not shown.
- the annular groove or channel in which the piston I3 slides has the above mentioned enlarged chamber I5 extending inwardly at the bottom of the guiding channel, and the piston is provided with a preferably integral and relatively wide radial flange I6 projecting inwardly from its lower end into said enlarged chamber to divide this chamber into a lower space below the flange and an annular, groovelike upper space I! above the flange.
- This wide 4 annular flange I6 has its inner edge slightly spaced from the inner wall of the chamber so that there is an open but restricted communication between the lower and upper spaces. Hence the working liquid entering the lower portion of the chamber through the passage or passages I9 will also enter the groove-like upper space II, and there will be a tendence of the liquid above the flange to be retained in the space II when the liquid below the flange is permitted for rapidly discharge upon the opening of the valves 25. This liquid will, on account of centrifugal force, remain in the upper space H, and it will consequently exercise a strong hydrostatic pressure tending to force the annular piston downwardly to open position and keep it there until liquid is again admitted to the chamber through the passages I9 for the reverse action.
- the groove-like upper space H is preferably made of angular shape in cross-section, being narrow vertically at its largest diameter and wider vertically at its smallest diameter. This may be done by forming the upper face of the flange l6 at its inner edge with an annular recess and forming a similar opposed recess in the portion of the inner part 29 forming the top of the enlarged chamber, as clearly shown in the drawings.
- I also preferably form in the piston I3 an inwardly-open, annular groove 33 which opens into the reduced or narrower outer portion of the upper space IT.
- This groove 33 forms a collecting pocket for any solid particles or impurities in the piston-actuating liquid. Such impurities will consequently not constitute any hinderance to the reciprocation of the piston I3.
- Discharge pipes or members 3!] for continuous discharge of semi-solid sludge may be arranged in the separator bowl.
- interchangeable parts 34 and 35 for replacement together with members 40 when worn may be provided in the peripheral slots II.
- All the functions for supplying piston actuating liquid and valve manoeuvering liquid may be operated manually, or be arranged for automatic operation.
- a centrifugal separator including a bowl adapted to be rotated to efiect continuous dis charge of liquid efiluents and the concentration of suspended solid material within the bowl, and provided with peripheral slots for the intermittent discharge of concentrated solid material, said bowl having a body with outer and inner portions between which is an annu .lr piston-receiving channel and an enlarged, annular chamber which extends inwardly at the bottom of said channel, an annular dischargecontrolling piston mounted in said channel for reciprocation therein against and away from a sealing surface to control the discharge of concentrated solid material from said peripheral slots, said piston being provided with a radial flange extending inwardly from its lower portion and into said chamber to divide the latter into a lower space below said flange and an upper, annular groove-like space above said flange, said upper and lower spaces being in open communication with each other around the inner edge of said flange and both being adapted to receive a piston-actuating liquid, the area of the flange in contact with the lower space being greater
Landscapes
- Centrifugal Separators (AREA)
Description
Dec. 11, 1951 A.-NYROP I SELF-DISCHARGING SLUDGE SEPARATOR Filed July 11. 1947 I Invenfor: WW
Affomg/s i atented Dec. 11 1951 UN-ITED STATES PATENT OFFICE SELF-DISCHARGIIGZZfSIDGE SEPARATOR Application July 11, 1947; SerialNp. 760,303 In Denmark July 4, 1942 Sectionl, Public "Law 690, August 8,1946 Patent expires July 4; 1962 3 Claims. l IL The present invention relates to a self-discharging sludge separator designed to separate sludge from one or two liquids.
More particularly the invention relates to centrifugal separators of the type in which the bowl is divided into two parts which are adapted to'undergo a relative axial movement at periodic intervals, to aiiord provision for discharge of sludge between the bowlpar ts. Such separators are described in my prior Patent No. 2,091,329.
In the separation or various fluids and sludge it is of importance that the slot, or the slots, at the periphery of the bowl, and through which the sludge is discharged, are opened and kept in their fully opened condition for a period sufficiently long to permit all the sludge to be discharged. The aim of the present invention is to provide means for attaining such a desired opening of the said slot or slots.
This arrangement ensures that coarse and tough sludge which otherwise will adhere to the sides of the separating drum is given a sufficient opening "of the slot, and sufficiently long time to be discharged from the bowl with as little resistance as possible.
In separators of the type in question it has been aimed to achieve a rapid opening or the peripheral slots by means "of a fluid and rapidly operating valves, but as the time of actual discharge is very short, certain diificulties have been experienced to open the slots to their full extent, because pressure within the separator bowl is decreased during the opening.
The present invention tends not only to provide a rapid opening of the peripheral slot or slots of the bowl, but likewise to ensure a free or full opening. 'l'his'can be attained by means of an axially disposed reciprocating member for closin said slots provided with an integral- -circular flange between which and a part oi the bowl is arranged a circular groove or space that will hold some of the fluid used for reciprocating the said member.
The fluid will remain in the circular groove on account of the centrifugal force, and will tend to actuate and force said reciprocating member into open position.
A complete understanding of the invention will be derived from the following detailed description with reference to the accompanying drawing, in which Fig. 1 shows an axial sectional view of a sludge separator according to the invention and Fig. 2 is a detail section showing a modification.
Referring to the drawing, 1 indicates the top part of a separator bowl which in conventional manner is screwedto the bottom parts of the bowl for instance by means of bolts A centre tube 2 has attached thereto a discharge ring 3 carrying distributing discs 6, separating plates 5-, and an insert 8 with wings extending into the separator bowl, serving to give the fluid to be treated the same rotationalspeed as the bowl parts. The "fluid to be separated is charged through a pipe I into the centre tube 2 from the lower end-of it is conveyed into the actual separating space. Thefiirid passes either round the lower end -of the "centre tube and from outside in between the discs 6, or it conveyed through apertures 43- in the lower end of the centre tube 2 upwardly through -distri butin'g holes '32 in the discs 6. During separa- 'tion the lighter components of the fluid will move centripetally between the discs and collect in the space interior to these, "and from here be discharged through the discharge rin 3-, whereas the heavier components of the fluid will pass round the exterior edge or the separa-e ting plates 5 and be discharged through one or several channels or spaces 44 above the said separating plates to the discharge ring '3'. These heavier iluid components pass an annular weir ii 'detachaloly connected to the upper bowl part 1. By inserting weirs of varying diameter it is possible to regulate the separation line in the bowl between heavy and light fluid components. If "the liquid only con'ta-insone kind of fluid the discharge over the weir may be closed.
During separation the solid component in the fluid, if heavier than the fluid, will collect in the space near the periphery of the bowl. The bowl has one or several slots it which are closed durin -separation of the solid components within the bowl by means of a reciprocable annular piston 1'3 mounted in an annular groove the bowl which piston periodically is operated to uncover the slots, thus allowing the sludge col-- lected in the separator bowl to be ejected by centrifugal "force. This annular piston t3 reciproca'tes as a piston in a =cyl-inder,'being guided vertically "in an annular groove or channel formed between the upright, outer, cylindrical portion of the lower part it of the body and an inner part 29 positioned within said lower part. It will be noted that the lower portion of this. fixed inner part 29 is of reduced diameter. to provide an enlarged annular chamber [:5 ex.- tending "inwardly from the bottom of the annular groove or channel in which the piston slides.
By means er a piston-actuating liquid conveyed to the space or chamber I and subjected to centrifugal force, the piston is forced upwardly against a gasket ID to seal the discharge slots II. The outer side of the upright portion of the piston I3 may be provided with integrally formed, upper and lower, flexible and resilient lips I2 and I3 which slide on the inner face of the upright cylindrical portion of the lower part I8 and serve as packing rings. Centrifugal force will throw the lips outwardly into sealing position. The inner face of the upright portion of the piston may be sealed by a lipped resilient packing ring 28 held in position on the inner part 29 by a suitable retaining ring as shown. These packings I2, Id and 28 are to prevent fluids from by-passing the piston. The piston-actuating liquid is sprayed from a tube or tubes 22 into a groove 2I and is by centrifugal force pressed into the bottom of the space or chamber I5 through channels I9.
During the periods in which the slots II are closed a tiny jet of liquid may be constantly sprayed into the groove 2I to provide hydraulic pressure in the space below the piston to ensure the slots I I being held closed during these periods.
As above noted it is important particularly when the separator is handling matter having solids of a sticky or adhesive nature, for the slots II to be opened quickly and fully. To aid in accomplishing that aim, I provide for the quick escape of the liquid beneath the piston so that the pressure within the separator may act on the obtuse edge 3| of the piston l3 to move it downwardly to open the slots II. To permit of such quick release of the liquid I provide one or more relatively large outlets or discharge passages 26, 26 from the bottom of the chamber I5 to the exterior. These passages are controlled by valves 25 which carry pistons 21 and which are of well-known type, being centrifugally operated to closed positions and being hydraulically operated to opened positions.
When the discharge slots II are to be opened, the operating liquid is sprayed from a tube 23 into a groove 45. By centrifugal force the liquid passes through channels 20 to the spaces at the outer ends of the cylinders in which the pistons 2I reciprocate, the pistons being thus forced inwardly to open the valves 25. The liquid in the space or chamber I5 may then discharge through the passages 26, 26 to release the pressure on the bottom of the piston I3, so that the pressure of the fluid and solid material in the separating section of the body on the edge 3| will cause the piston to move downwardly to open the slots II. The control of the operating liquid may be a four-way valve, not shown.
As the pressure in the separating compartment on the edge 3| of the piston decreases as soon as the slots II open, the displacement of and the maintenance of the piston I3 in its open position will be uncertain even when the displacement or opening movement is rapid. To remedy this, the annular groove or channel in which the piston I3 slides has the above mentioned enlarged chamber I5 extending inwardly at the bottom of the guiding channel, and the piston is provided with a preferably integral and relatively wide radial flange I6 projecting inwardly from its lower end into said enlarged chamber to divide this chamber into a lower space below the flange and an annular, groovelike upper space I! above the flange. This wide 4 annular flange I6 has its inner edge slightly spaced from the inner wall of the chamber so that there is an open but restricted communication between the lower and upper spaces. Hence the working liquid entering the lower portion of the chamber through the passage or passages I9 will also enter the groove-like upper space II, and there will be a tendence of the liquid above the flange to be retained in the space II when the liquid below the flange is permitted for rapidly discharge upon the opening of the valves 25. This liquid will, on account of centrifugal force, remain in the upper space H, and it will consequently exercise a strong hydrostatic pressure tending to force the annular piston downwardly to open position and keep it there until liquid is again admitted to the chamber through the passages I9 for the reverse action. It will be noted that the area of the flange I6 in contact with the lower space is greater than that in contact with the upper space. I have found that this action of the substantial body of liquid retained by centrifugal force in the upper space I'I, not only aids the quick opening of the piston to its fully opened position but tends to hold the piston in such fully open position so that even very tough, sticky and course solid matter will be satisfactorily ejected through the slots I I.
The groove-like upper space H is preferably made of angular shape in cross-section, being narrow vertically at its largest diameter and wider vertically at its smallest diameter. This may be done by forming the upper face of the flange l6 at its inner edge with an annular recess and forming a similar opposed recess in the portion of the inner part 29 forming the top of the enlarged chamber, as clearly shown in the drawings. By thus widening the inner portion of the space I! a vertically thick body of liquid in the groove-like space is attained, and consequently there will be a greater downward pressure on the flange I6 when liquid is quickly discharged from the space beneath the flange. As the piston lowers, the upper space H widens vertically and hence the wider inner portion will act as a reservoir for the narrower outer portion, and a considerable amount of the liquid will be retained by centrifugal force above the flange I5.
I also preferably form in the piston I3 an inwardly-open, annular groove 33 which opens into the reduced or narrower outer portion of the upper space IT. This groove 33 forms a collecting pocket for any solid particles or impurities in the piston-actuating liquid. Such impurities will consequently not constitute any hinderance to the reciprocation of the piston I3. Discharge pipes or members 3!] for continuous discharge of semi-solid sludge may be arranged in the separator bowl.
As shown in Fig. 2 interchangeable parts 34 and 35 for replacement together with members 40 when worn, may be provided in the peripheral slots II.
All the functions for supplying piston actuating liquid and valve manoeuvering liquid may be operated manually, or be arranged for automatic operation.
It will readily be understood that the construction can be modified in various manners within the scope of the invention as defined in the following claims.
I claim:
1. A centrifugal separator, including a bowl adapted to be rotated to efiect continuous dis charge of liquid efiluents and the concentration of suspended solid material within the bowl, and provided with peripheral slots for the intermittent discharge of concentrated solid material, said bowl having a body with outer and inner portions between which is an annu .lr piston-receiving channel and an enlarged, annular chamber which extends inwardly at the bottom of said channel, an annular dischargecontrolling piston mounted in said channel for reciprocation therein against and away from a sealing surface to control the discharge of concentrated solid material from said peripheral slots, said piston being provided with a radial flange extending inwardly from its lower portion and into said chamber to divide the latter into a lower space below said flange and an upper, annular groove-like space above said flange, said upper and lower spaces being in open communication with each other around the inner edge of said flange and both being adapted to receive a piston-actuating liquid, the area of the flange in contact with the lower space being greater than that in contact with the upper space, means for admitting a piston-actuating liquid. into said lower space to act on the bottom of said flange to move said piston upwardly to sealing position and to enter said upper space around the inner edge of said flange, valve-controlled, quick-escape, liquid passages leading from said lower space to permit the quick discharge of liquid beneath the flange during motion of the piston downwardly to discharge position for concentrated solids, and valves for controlling said discharge passages, said valves being centrifugally actuated to closed positions and hydraulically operated to open positions, said upper groove-like space being so proportioned and arranged that when said valves are hydraulically operated to permit of the quick escape of liquid beneath the flange, a substantial body of liquid will be retained by centrifugal force in the space above said flange and will exert a hydrostatic pressure tending to force said flange downwardly to assist in the quick and full opening of said piston.
2. The structure of claim 1 in which said upper groove-like annular space has an angular cross-section, being narrow in a vertical direction at its larger diameter and wide in a vertical direction at its smaller diameter.
3. The structure of claim 1 in which said piston is formed with an inwardly open annular groove to collect impurities in the piston-actuating fluid, said groove opening into said groove-like upper space at its largest diameter.
AAGE NYROP.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 2,091,329 Nyrop Aug. 31, 1937 2,126,864 Bath Aug. 16, 1938 2,178,547 Bjornstjerna Nov. 7, 1939 2,209,554 Bath July 30, 1940 FOREIGN PATENTS Number Country Date 715,701 France Sept. 29, 1931 400,809 Great Britain Nov. 2, 1933
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DK2578484X | 1942-07-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2578484A true US2578484A (en) | 1951-12-11 |
Family
ID=8158531
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US760303A Expired - Lifetime US2578484A (en) | 1942-07-04 | 1947-07-11 | Self-discharging sludge separator |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2578484A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2862659A (en) * | 1956-05-31 | 1958-12-02 | Nyrop Aage | Centrifugal separator |
| US2873910A (en) * | 1954-03-13 | 1959-02-17 | Westfalia Separator Ag | Sludge-discharging centrifugal separators |
| US3189267A (en) * | 1960-04-20 | 1965-06-15 | Separator Ab | Sludge centrifuge |
| US3239136A (en) * | 1962-05-07 | 1966-03-08 | George N Hein | Centrifuge and centrifuge head for separating constituents of a liquid and a liner therefor |
| US3244363A (en) * | 1959-06-24 | 1966-04-05 | George N Hein | Centrifuge apparatus and bag therefor |
| US3261546A (en) * | 1962-10-29 | 1966-07-19 | Pfaudler Permutit Inc | Method for clarifying fats and oils |
| DE1297036B (en) * | 1966-11-22 | 1969-06-04 | Westfalia Separator Ag | Plate insert for self-cleaning centrifugal drums |
| US3630431A (en) * | 1969-06-18 | 1971-12-28 | Mitsubishi Kakoki Kk | Valve-discharge disc centrifuge |
| US3940056A (en) * | 1973-02-27 | 1976-02-24 | Westfalia Separator Ag | Self-cleaning centrifuge drum |
| US4069969A (en) * | 1976-09-28 | 1978-01-24 | Mitsubishi Kakoki Kaisha, Ltd. | Automatic three stage centrifugal sludge separator |
| US4410317A (en) * | 1981-05-15 | 1983-10-18 | Westfalia Separator Ag | Self-discharging centrifugal drum |
| US9387491B2 (en) * | 2013-03-06 | 2016-07-12 | Alfa Laval Corporate Ab | Centrifugal separator having a valve body provided in an outlet channel |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR715701A (en) * | 1931-04-20 | 1931-12-08 | Separator Ab | Separator with intermittent discharge of sludge or impurities |
| GB400809A (en) * | 1933-01-18 | 1933-11-02 | Aage Nyrop | Improvements in centrifugal separators |
| US2091329A (en) * | 1933-01-18 | 1937-08-31 | Nyrop Aage | Centrifugal separator |
| US2126864A (en) * | 1935-02-27 | 1938-08-16 | Sharples Specialty Co | Centrifugal machine |
| US2178547A (en) * | 1936-06-26 | 1939-11-07 | Laval Separator Co De | Centrifugal separator |
| US2209554A (en) * | 1936-12-10 | 1940-07-30 | Sharples Corp | Centrifugal separator |
-
1947
- 1947-07-11 US US760303A patent/US2578484A/en not_active Expired - Lifetime
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR715701A (en) * | 1931-04-20 | 1931-12-08 | Separator Ab | Separator with intermittent discharge of sludge or impurities |
| GB400809A (en) * | 1933-01-18 | 1933-11-02 | Aage Nyrop | Improvements in centrifugal separators |
| US2091329A (en) * | 1933-01-18 | 1937-08-31 | Nyrop Aage | Centrifugal separator |
| US2126864A (en) * | 1935-02-27 | 1938-08-16 | Sharples Specialty Co | Centrifugal machine |
| US2178547A (en) * | 1936-06-26 | 1939-11-07 | Laval Separator Co De | Centrifugal separator |
| US2209554A (en) * | 1936-12-10 | 1940-07-30 | Sharples Corp | Centrifugal separator |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2873910A (en) * | 1954-03-13 | 1959-02-17 | Westfalia Separator Ag | Sludge-discharging centrifugal separators |
| US2862659A (en) * | 1956-05-31 | 1958-12-02 | Nyrop Aage | Centrifugal separator |
| US3244363A (en) * | 1959-06-24 | 1966-04-05 | George N Hein | Centrifuge apparatus and bag therefor |
| US3189267A (en) * | 1960-04-20 | 1965-06-15 | Separator Ab | Sludge centrifuge |
| US3239136A (en) * | 1962-05-07 | 1966-03-08 | George N Hein | Centrifuge and centrifuge head for separating constituents of a liquid and a liner therefor |
| US3261546A (en) * | 1962-10-29 | 1966-07-19 | Pfaudler Permutit Inc | Method for clarifying fats and oils |
| DE1297036B (en) * | 1966-11-22 | 1969-06-04 | Westfalia Separator Ag | Plate insert for self-cleaning centrifugal drums |
| US3630431A (en) * | 1969-06-18 | 1971-12-28 | Mitsubishi Kakoki Kk | Valve-discharge disc centrifuge |
| US3940056A (en) * | 1973-02-27 | 1976-02-24 | Westfalia Separator Ag | Self-cleaning centrifuge drum |
| US4069969A (en) * | 1976-09-28 | 1978-01-24 | Mitsubishi Kakoki Kaisha, Ltd. | Automatic three stage centrifugal sludge separator |
| US4410317A (en) * | 1981-05-15 | 1983-10-18 | Westfalia Separator Ag | Self-discharging centrifugal drum |
| US9387491B2 (en) * | 2013-03-06 | 2016-07-12 | Alfa Laval Corporate Ab | Centrifugal separator having a valve body provided in an outlet channel |
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