US3593915A - Controlled desludging of centrifugal separators - Google Patents
Controlled desludging of centrifugal separators Download PDFInfo
- Publication number
- US3593915A US3593915A US820421A US3593915DA US3593915A US 3593915 A US3593915 A US 3593915A US 820421 A US820421 A US 820421A US 3593915D A US3593915D A US 3593915DA US 3593915 A US3593915 A US 3593915A
- Authority
- US
- United States
- Prior art keywords
- sludge
- drum
- bowl
- float
- shaft
- 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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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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
- B04B11/04—Periodical feeding or discharging; Control arrangements therefor
- B04B11/043—Load indication with or without control arrangements
Definitions
- a self-cleaning liquid-solids separator with valve means such as a controllable sliding-ring valve, for discharging sludge through the periphery of the bowl is equipped with a float that will sense the liquid-solids interface in the bowl during operation.
- a sensing device e.g. an electric coil, is attached to the shaft of the drum and senses the position of an elongated member or rod attached to the float and extending inwardly towards the shaft.
- the sensing device activates opening of the sludge discharge valve means, and if desired, after a certain amount of sludge has been discharged, the closing of the valve means.
- V CONTROLLED DESLUDGING OF CENTRIFUGAL SEPARATORS PRlOR ART Control apparatus for self-cleaning separators which automatically cause sludge discharge ejection or orifices in the periphery of the drum to open according to a specific time program. Since the filling of the sludge chamber depends upon the solid content of the mixture, the throughput of the drum and the capacity of the sludge chamber, it can happen that the sludge ejection orifices may be opened too earlyor too late when the solid content in the mixture varies, when the throughput varies, or when the drum is not completely emptied in the preceding desludging operation.
- Every control system has its advantages and disadvantages. Electrical systems have performed well as regards sensitivity and reliability of response. Mechanically, however, they are usually very delicate and hence poorly suited for the severe conditions of separator operation. Also, nearly all electrical components require an insulated mounting, and since liquid mixtures are as a rule electrically conductive, liquid spray and condensation might imperil the insulation when the com ponents are used in a separator. Another difficulty in the use of electrical systems for sensing sludge level in a centrifugal separating drum is caused by the fact that the drum is rotating and the controls and switchgear are located outside of the drum.
- sliprings are generally used, whichhave to be mounted on the shaft in an insulated manner. Aside from the fact that insulated mounting presents difficulties for the reasons stated above, they can also interfere with and be damaged by the disassembly and reassembly of the drum.
- U.S. Pat. No. 3,189,268 discloses a system wherein the shifting of the boundary surface between two components of the mixture being separated varies the capacity between two insulated wires and the drum when the boundary surface lies within the radial reach of the wires.
- the invention is a system for the automatic initiation of the desludging of a centrifugal separator. It operates with equal reliability with all mixtures and in all types of separators, even in so-called hermetic separators. An electrical transducer instead of sliprings is used as the sensing element.
- the system according to the invention is characterized by a float which is disposed in the sludge chamber of the drum and is displaceable toward and away from the axis of rotation. lt is suitably guided in its movements in the drum, and is provided on its inner extremity with a means for influencing an electrical or magnetic field produced by a condenser or coil affixed to a structural part extending into the drum.
- a condenser or coil affixed to a structural part extending into the drum.
- the lower part of the drum 1 and the drum cover are held together by a ring 3 and its retaining ring 3a.
- the lower part of the drum is provided with sludge ejection orifices 4, shown closed on the right side and open on the left. These orifices are periodically opened by a slidingring valve 5 in a known manner.
- a float 8 In the sludge chamber 6, out side of the plates 7, there is disposed a float 8, which is guided by means of a rod 9 in a bore in the drum cover 2.
- the float body is specifically lighter than the heaviest component of the mixture to be separated and immersed only partially in the latter. As the level of the heaviest component or sludge increases, the float is displaced toward the axis of rotation.
- Rod 9 has on its inner extremity an appropriately shaped body 10 of suitable material, so that, when the float 8 is displaced inwardly, it affects the capacity of a condenser or the inductance of a coil 11.
- a coil 11 is fastened to the stationary infeed tube 12, and the body 10 cooperates with it according to the position of the float 8.
- Coil 11 is connected outside of the drum to other electrical elements in the box 13, which start the desludging of the drum when a certain inductance value in coil 1 is reached, doing so, for example, by closing an electrically operated valve 14 in the mixture-feeding tube 15 and opening valve 16 in a hydraulic fluid line 17, the fluid causing valve 5 to open.
- the positions of these valves can be reversed.
- a self-cleaning liquid-solids centrifugal separator having a rotatable bowl with a sludge discharge orifice on the periphery thereof adapted to be opened and closed during the operation of the separator; an improvement for initiating the desludging of said separator comprising a float means within said bowl and adapted to sense the liquid-solids interface in said bowl, said float means including an elongated member disposed inwardly towards the axis of revolution of said bowl, sensing means for sensing the position of the end of said elongated member relative to axis of revolution, and control means operatively connected to said sensing means and adapted to open said sludge discharge orifice when the builtup solids in said bowl reaches a predetennined level.
- sensing means includes an element attached to a fixed member within said bowl and extends around said axis of revolution and is adapted to sense changes in said electromagnetic field induced by the position of the end of said elongated member relative thereto.
Landscapes
- Centrifugal Separators (AREA)
Abstract
A self-cleaning liquid-solids separator with valve means, such as a controllable sliding-ring valve, for discharging sludge through the periphery of the bowl is equipped with a float that will sense the liquid-solids interface in the bowl during operation. A sensing device, e.g. an electric coil, is attached to the shaft of the drum and senses the position of an elongated member or rod attached to the float and extending inwardly towards the shaft. When the end of the rod approaches close enough to the shaft, which indicates the sludge has built up to a predetermined level, the sensing device activates opening of the sludge discharge valve means, and if desired, after a certain amount of sludge has been discharged, the closing of the valve means.
Description
United States Patent Inventor Appl. No.
Filed Patented Assignee Priority Peter Steinacker Oelde, Westphalia, Germany 820,421
Apr. 30, 1969 July 20, 1971 Westfalia Separator AG. Oelde, Westphalia, Germany Sept. 25, 1968 Germany CONTROLLED DESLUDGING OF CENTRIFUGAL SEPARATORS 4 Claims, 1 Drawing Fig.
u.s. Cl 233/20 Int. Cl B04b 11/00 Field ofSearch 233/19,20,
OPEN POSITION Primary Examiner-Robert W. Jenkins Attorney-Burgess, Dinklage & Sprung ABSTRACT: A self-cleaning liquid-solids separator with valve means, such as a controllable sliding-ring valve, for discharging sludge through the periphery of the bowl is equipped with a float that will sense the liquid-solids interface in the bowl during operation. A sensing device, e.g. an electric coil, is attached to the shaft of the drum and senses the position of an elongated member or rod attached to the float and extending inwardly towards the shaft. When the end of the rod approaches close enough to the shaft, which indicates the sludge has built up to a predetermined level, the sensing device activates opening of the sludge discharge valve means, and if desired, after a certain amount of sludge has been discharged, the closing of the valve means.
PATENTED JULZO I97! OPEN POSITION R E K m mm TE NT S V mm T E D.
BURGESS. D\NKLAGE & SPRUNG ATTORNEYS.
V CONTROLLED DESLUDGING OF CENTRIFUGAL SEPARATORS PRlOR ART Control apparatus for self-cleaning separators are known which automatically cause sludge discharge ejection or orifices in the periphery of the drum to open according to a specific time program. Since the filling of the sludge chamber depends upon the solid content of the mixture, the throughput of the drum and the capacity of the sludge chamber, it can happen that the sludge ejection orifices may be opened too earlyor too late when the solid content in the mixture varies, when the throughput varies, or when the drum is not completely emptied in the preceding desludging operation.
In the first case, too much of the desired liquid is lost in the desludging operation; in the second case the sludge stratum grows into the plate stack, impairing the flow of the liquid and hence the clarifying action of the drum.
ln automating the operation of separators, the tendency has been to construct the drum of the separator so that it starts the desludging action itself when the level in the sludge chamber has reached a predetermined point. A self-controlling system that operates independently of time in this manner obviates the above-named disadvantages of time control, and apparatus of this sort have previously been described in U.S. Pat. Nos. 3,167,509 and 3,301,476.
Every control system has its advantages and disadvantages. Electrical systems have performed well as regards sensitivity and reliability of response. Mechanically, however, they are usually very delicate and hence poorly suited for the severe conditions of separator operation. Also, nearly all electrical components require an insulated mounting, and since liquid mixtures are as a rule electrically conductive, liquid spray and condensation might imperil the insulation when the com ponents are used in a separator. Another difficulty in the use of electrical systems for sensing sludge level in a centrifugal separating drum is caused by the fact that the drum is rotating and the controls and switchgear are located outside of the drum. When an element that responds to changes in sludge level is installed in the drum, the power to operate it must be delivered to it from the outside and the signal it emits must be transmitted to the outside. For this purpose, sliprings are generally used, whichhave to be mounted on the shaft in an insulated manner. Aside from the fact that insulated mounting presents difficulties for the reasons stated above, they can also interfere with and be damaged by the disassembly and reassembly of the drum.
U.S. Pat. No. 3,189,268 discloses a system wherein the shifting of the boundary surface between two components of the mixture being separated varies the capacity between two insulated wires and the drum when the boundary surface lies within the radial reach of the wires.
ln this system the use of sliprings is avoided by connecting a second condenser in series with the sensing capacitor, one plate of which is attached to the rotating drum and the other to the stationary housing.
This prior art system, however, is evidently suitable only for mixtures of high ohmic resistance, such as may be constituted by mixtures of oil and water. In the case of liquids having relatively high conductivity, capacitive measurements are not easily possible.
' 5 THIS INVENTION The invention is a system for the automatic initiation of the desludging of a centrifugal separator. It operates with equal reliability with all mixtures and in all types of separators, even in so-called hermetic separators. An electrical transducer instead of sliprings is used as the sensing element.
The system according to the invention is characterized by a float which is disposed in the sludge chamber of the drum and is displaceable toward and away from the axis of rotation. lt is suitably guided in its movements in the drum, and is provided on its inner extremity with a means for influencing an electrical or magnetic field produced by a condenser or coil affixed to a structural part extending into the drum. The disadvantages described above are eliminated by the cooperation of a stationary electrical part with a mechanical part that rotates with the drum.
THE DRAWlNG An example of one embodiment of the invention is represented in the drawing.
DESCRIPTION AND EXAMPLE With reference to the drawing, the lower part of the drum 1 and the drum cover are held together by a ring 3 and its retaining ring 3a. The lower part of the drum is provided with sludge ejection orifices 4, shown closed on the right side and open on the left. These orifices are periodically opened by a slidingring valve 5 in a known manner. In the sludge chamber 6, out side of the plates 7, there is disposed a float 8, which is guided by means of a rod 9 in a bore in the drum cover 2. The float body is specifically lighter than the heaviest component of the mixture to be separated and immersed only partially in the latter. As the level of the heaviest component or sludge increases, the float is displaced toward the axis of rotation.
In the example, a coil 11 is fastened to the stationary infeed tube 12, and the body 10 cooperates with it according to the position of the float 8. Coil 11 is connected outside of the drum to other electrical elements in the box 13, which start the desludging of the drum when a certain inductance value in coil 1 is reached, doing so, for example, by closing an electrically operated valve 14 in the mixture-feeding tube 15 and opening valve 16 in a hydraulic fluid line 17, the fluid causing valve 5 to open. At the end of a preset time of when the sludge falls to a predetermined level, the positions of these valves can be reversed.
What 1 claim is:
I. In a self-cleaning liquid-solids centrifugal separator having a rotatable bowl with a sludge discharge orifice on the periphery thereof adapted to be opened and closed during the operation of the separator; an improvement for initiating the desludging of said separator comprising a float means within said bowl and adapted to sense the liquid-solids interface in said bowl, said float means including an elongated member disposed inwardly towards the axis of revolution of said bowl, sensing means for sensing the position of the end of said elongated member relative to axis of revolution, and control means operatively connected to said sensing means and adapted to open said sludge discharge orifice when the builtup solids in said bowl reaches a predetennined level.
2. The improvement of claim 1 wherein said bowl, is conical and said elongated member is supported by and extends along the inner conical periphery of said bowl towards said axis of revolution.
3. The improvement of claim 2 wherein said sensing means includes an element attached to a fixed member within said bowl and extends around said axis of revolution and is adapted to sense changes in said electromagnetic field induced by the position of the end of said elongated member relative thereto.
4. The improvement of claim 3 wherein said element is an electric coil and said end of elongated member inductively couples therewith.
Claims (3)
- 2. The improvement of claim 1 wherein said bowl, is conical and said elongated member is supported by and extends along the inner conical periphery of said bowl towards said axis of revolution.
- 3. The improvement of claim 2 wherein said sensing means includes an element attached to a fixed member within said bowl and extends around said axis of revolution and is adapted to sense changes in said electromagnetic field induced by the position of the end of said elongated member relative thereto.
- 4. The improvement of claim 3 wherein said element is an electric coil and said end of elongated member inductively couples therewith.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19681782612 DE1782612B1 (en) | 1968-09-25 | 1968-09-25 | DEVICE FOR INITIATING THE DESludging of SELF-CLEANING MUD CENTRIFUGES |
Publications (1)
Publication Number | Publication Date |
---|---|
US3593915A true US3593915A (en) | 1971-07-20 |
Family
ID=5705127
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US820421A Expired - Lifetime US3593915A (en) | 1968-09-25 | 1969-04-30 | Controlled desludging of centrifugal separators |
Country Status (5)
Country | Link |
---|---|
US (1) | US3593915A (en) |
DE (1) | DE1782612B1 (en) |
FR (1) | FR1596305A (en) |
GB (1) | GB1214228A (en) |
SE (1) | SE338281B (en) |
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3765599A (en) * | 1970-10-02 | 1973-10-16 | Westfalia Separator Ag | Self cleaning centrifuge drum with stepwise variable closing pressure |
US3823868A (en) * | 1972-03-01 | 1974-07-16 | M Baram | Sludge ejecting centrifuge |
US3938734A (en) * | 1973-12-21 | 1976-02-17 | Westfalia Separator Ag | Controlling system for the displacement of the specifically lighter liquid components from a self-emptying separator |
US3976242A (en) * | 1974-07-27 | 1976-08-24 | Westfalia Separator Aktiengesellschaft | Self-emptying clarifying separator having a foam-free removal of the clarified liquid by means of a paring disk and an automatically operating system for detecting the level of the solids in the sludge chamber |
US3986663A (en) * | 1973-01-08 | 1976-10-19 | Alfa-Laval Ab | Centrifugal separator with sensing means |
US4288029A (en) * | 1978-12-06 | 1981-09-08 | Klockner-Humboldt-Deutz Ag | Separator with pressure-responsive discharge |
US4347971A (en) * | 1977-03-03 | 1982-09-07 | Joy Manufacturing Company | Centrifuge apparatus |
US4392846A (en) * | 1981-05-18 | 1983-07-12 | Joy Manufacturing Company | Centrifuge apparatus |
US4432748A (en) * | 1976-09-03 | 1984-02-21 | Joy Manufacturing Company | Centrifuge apparatus and method of operating a centrifuge |
US4525155A (en) * | 1983-04-20 | 1985-06-25 | Alfa-Laval Marine And Powering Engineering Ab | Centrifugal separator and method of operating the same |
US5800330A (en) * | 1994-07-22 | 1998-09-01 | Alfa Laval Ab | Method and equipment for monitoring a centrifugal separator |
US6358193B1 (en) * | 1997-09-29 | 2002-03-19 | Alfa Laval Ab | Regulation device for a centrifugal separator to control discharge from outlets |
US6837842B1 (en) * | 1999-03-08 | 2005-01-04 | Alfa Laval Ab | Method and device for indicating an undesired operation condition of a centrifugal separator |
US20080011684A1 (en) * | 2005-02-07 | 2008-01-17 | Dorian Randel E | Apparatus and method for preparing platelet rich plasma and concentrates thereof |
US7708152B2 (en) | 2005-02-07 | 2010-05-04 | Hanuman Llc | Method and apparatus for preparing platelet rich plasma and concentrates thereof |
US7824559B2 (en) | 2005-02-07 | 2010-11-02 | Hanumann, LLC | Apparatus and method for preparing platelet rich plasma and concentrates thereof |
US8012077B2 (en) | 2008-05-23 | 2011-09-06 | Biomet Biologics, Llc | Blood separating device |
US8187475B2 (en) | 2009-03-06 | 2012-05-29 | Biomet Biologics, Llc | Method and apparatus for producing autologous thrombin |
US8337711B2 (en) | 2008-02-29 | 2012-12-25 | Biomet Biologics, Llc | System and process for separating a material |
US20130029828A1 (en) * | 2010-01-29 | 2013-01-31 | Alfa Laval Corporate Ab | System comprising centrifugal separator and method for controlling such a system |
US20130065744A1 (en) * | 2010-03-19 | 2013-03-14 | Per Karlsson | Device and method for monitoring and adjusting the radial position of an interface layer in a nozzle centrifuge |
CN104959244A (en) * | 2015-07-23 | 2015-10-07 | 柳州永生好茶油有限公司 | Automatic cleaning-type centrifuge used for producing tea oil |
CN105032635A (en) * | 2015-07-23 | 2015-11-11 | 柳州永生好茶油有限公司 | Manual control cleaning centrifuge used for tea oil production |
US9713810B2 (en) | 2015-03-30 | 2017-07-25 | Biomet Biologics, Llc | Cell washing plunger using centrifugal force |
US9757721B2 (en) | 2015-05-11 | 2017-09-12 | Biomet Biologics, Llc | Cell washing plunger using centrifugal force |
US9975127B2 (en) | 2013-05-27 | 2018-05-22 | Alfa Laval Corporate Ab | Centrifugal separator and method for determining suitable moment for removal of heavy phase content |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE408838B (en) * | 1975-02-04 | 1979-07-09 | Prazska Akumulatorka Np | PROCEDURE FOR THE MANUFACTURE OF ACCUMULATOR ELECTRODES CONSISTING OF A MIXTURE OF AN ACTIVE SUBSTANCE AND A PLASTIC AND OF A POWER DISCHARGE |
DE102015005226B4 (en) | 2015-04-23 | 2019-06-27 | Mann+Hummel Gmbh | Rotor of a fluid centrifuge with indicator device |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3167509A (en) * | 1961-06-13 | 1965-01-26 | Westfalia Separator Ag | Centrifugal separator |
US3189268A (en) * | 1961-12-22 | 1965-06-15 | Ab | Device for determining the position of the interface between two separated components in a centrifugal separator |
US3301476A (en) * | 1963-01-26 | 1967-01-31 | Westfalia Separator Ag | Apparatus for signaling a predetermined level in the sludge chamber of a centrifugaldrum |
-
1968
- 1968-09-25 DE DE19681782612 patent/DE1782612B1/en active Pending
- 1968-12-23 FR FR1596305D patent/FR1596305A/fr not_active Expired
-
1969
- 1969-03-14 SE SE03543/69A patent/SE338281B/xx unknown
- 1969-04-30 US US820421A patent/US3593915A/en not_active Expired - Lifetime
- 1969-07-28 GB GB37777/69A patent/GB1214228A/en not_active Expired
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3167509A (en) * | 1961-06-13 | 1965-01-26 | Westfalia Separator Ag | Centrifugal separator |
US3189268A (en) * | 1961-12-22 | 1965-06-15 | Ab | Device for determining the position of the interface between two separated components in a centrifugal separator |
US3301476A (en) * | 1963-01-26 | 1967-01-31 | Westfalia Separator Ag | Apparatus for signaling a predetermined level in the sludge chamber of a centrifugaldrum |
Cited By (36)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3765599A (en) * | 1970-10-02 | 1973-10-16 | Westfalia Separator Ag | Self cleaning centrifuge drum with stepwise variable closing pressure |
US3823868A (en) * | 1972-03-01 | 1974-07-16 | M Baram | Sludge ejecting centrifuge |
US3986663A (en) * | 1973-01-08 | 1976-10-19 | Alfa-Laval Ab | Centrifugal separator with sensing means |
US3938734A (en) * | 1973-12-21 | 1976-02-17 | Westfalia Separator Ag | Controlling system for the displacement of the specifically lighter liquid components from a self-emptying separator |
US3976242A (en) * | 1974-07-27 | 1976-08-24 | Westfalia Separator Aktiengesellschaft | Self-emptying clarifying separator having a foam-free removal of the clarified liquid by means of a paring disk and an automatically operating system for detecting the level of the solids in the sludge chamber |
US4432748A (en) * | 1976-09-03 | 1984-02-21 | Joy Manufacturing Company | Centrifuge apparatus and method of operating a centrifuge |
US4347971A (en) * | 1977-03-03 | 1982-09-07 | Joy Manufacturing Company | Centrifuge apparatus |
US4288029A (en) * | 1978-12-06 | 1981-09-08 | Klockner-Humboldt-Deutz Ag | Separator with pressure-responsive discharge |
US4392846A (en) * | 1981-05-18 | 1983-07-12 | Joy Manufacturing Company | Centrifuge apparatus |
US4525155A (en) * | 1983-04-20 | 1985-06-25 | Alfa-Laval Marine And Powering Engineering Ab | Centrifugal separator and method of operating the same |
US5800330A (en) * | 1994-07-22 | 1998-09-01 | Alfa Laval Ab | Method and equipment for monitoring a centrifugal separator |
US6358193B1 (en) * | 1997-09-29 | 2002-03-19 | Alfa Laval Ab | Regulation device for a centrifugal separator to control discharge from outlets |
US6837842B1 (en) * | 1999-03-08 | 2005-01-04 | Alfa Laval Ab | Method and device for indicating an undesired operation condition of a centrifugal separator |
US7824559B2 (en) | 2005-02-07 | 2010-11-02 | Hanumann, LLC | Apparatus and method for preparing platelet rich plasma and concentrates thereof |
US7708152B2 (en) | 2005-02-07 | 2010-05-04 | Hanuman Llc | Method and apparatus for preparing platelet rich plasma and concentrates thereof |
US20080011684A1 (en) * | 2005-02-07 | 2008-01-17 | Dorian Randel E | Apparatus and method for preparing platelet rich plasma and concentrates thereof |
US7866485B2 (en) | 2005-02-07 | 2011-01-11 | Hanuman, Llc | Apparatus and method for preparing platelet rich plasma and concentrates thereof |
US7987995B2 (en) | 2005-02-07 | 2011-08-02 | Hanuman, Llc | Method and apparatus for preparing platelet rich plasma and concentrates thereof |
US8096422B2 (en) | 2005-02-07 | 2012-01-17 | Hanuman Llc | Apparatus and method for preparing platelet rich plasma and concentrates thereof |
US8105495B2 (en) | 2005-02-07 | 2012-01-31 | Hanuman, Llc | Method for preparing platelet rich plasma and concentrates thereof |
US8133389B2 (en) | 2005-02-07 | 2012-03-13 | Hanuman, Llc | Method and apparatus for preparing platelet rich plasma and concentrates thereof |
US20130196425A1 (en) * | 2008-02-29 | 2013-08-01 | Biomet Biologics, Llc | System and Process for Separating a Material |
US8801586B2 (en) * | 2008-02-29 | 2014-08-12 | Biomet Biologics, Llc | System and process for separating a material |
US8337711B2 (en) | 2008-02-29 | 2012-12-25 | Biomet Biologics, Llc | System and process for separating a material |
US8012077B2 (en) | 2008-05-23 | 2011-09-06 | Biomet Biologics, Llc | Blood separating device |
US8783470B2 (en) | 2009-03-06 | 2014-07-22 | Biomet Biologics, Llc | Method and apparatus for producing autologous thrombin |
US8187475B2 (en) | 2009-03-06 | 2012-05-29 | Biomet Biologics, Llc | Method and apparatus for producing autologous thrombin |
US20130029828A1 (en) * | 2010-01-29 | 2013-01-31 | Alfa Laval Corporate Ab | System comprising centrifugal separator and method for controlling such a system |
US9186687B2 (en) * | 2010-01-29 | 2015-11-17 | Alfa Laval Corporate Ab | Centrifugal separator with pressure or recirculation control or monitoring devices |
US20130065744A1 (en) * | 2010-03-19 | 2013-03-14 | Per Karlsson | Device and method for monitoring and adjusting the radial position of an interface layer in a nozzle centrifuge |
US8702576B2 (en) * | 2010-03-19 | 2014-04-22 | Alfa Laval Corporate Ab | Device and method for monitoring and adjusting the radial position of an interface layer in a nozzle centrifuge |
US9975127B2 (en) | 2013-05-27 | 2018-05-22 | Alfa Laval Corporate Ab | Centrifugal separator and method for determining suitable moment for removal of heavy phase content |
US9713810B2 (en) | 2015-03-30 | 2017-07-25 | Biomet Biologics, Llc | Cell washing plunger using centrifugal force |
US9757721B2 (en) | 2015-05-11 | 2017-09-12 | Biomet Biologics, Llc | Cell washing plunger using centrifugal force |
CN104959244A (en) * | 2015-07-23 | 2015-10-07 | 柳州永生好茶油有限公司 | Automatic cleaning-type centrifuge used for producing tea oil |
CN105032635A (en) * | 2015-07-23 | 2015-11-11 | 柳州永生好茶油有限公司 | Manual control cleaning centrifuge used for tea oil production |
Also Published As
Publication number | Publication date |
---|---|
FR1596305A (en) | 1970-06-15 |
GB1214228A (en) | 1970-12-02 |
DE1782612B1 (en) | 1971-05-19 |
SE338281B (en) | 1971-08-30 |
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