EP2401087B1 - Centrifugal separator and method for separating - Google Patents

Centrifugal separator and method for separating Download PDF

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Publication number
EP2401087B1
EP2401087B1 EP10714387.7A EP10714387A EP2401087B1 EP 2401087 B1 EP2401087 B1 EP 2401087B1 EP 10714387 A EP10714387 A EP 10714387A EP 2401087 B1 EP2401087 B1 EP 2401087B1
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EP
European Patent Office
Prior art keywords
liquid
space
separating chamber
interface layer
rotor
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.)
Active
Application number
EP10714387.7A
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German (de)
English (en)
French (fr)
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EP2401087A1 (en
Inventor
Lasse Hurnasti
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Alfa Laval Corporate AB
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Alfa Laval Corporate AB
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Publication of EP2401087A1 publication Critical patent/EP2401087A1/en
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    • 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
    • B04B1/04—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
    • B04B1/08—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape
    • 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
    • B04B1/12—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 continuous discharge
    • 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
    • B04B11/02—Continuous feeding or discharging; Control arrangements therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B13/00—Control arrangements specially designed for centrifuges; Programme control of centrifuges
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B13/00—Control arrangements specially designed for centrifuges; Programme control of centrifuges
    • B04B2013/006—Interface detection or monitoring of separated components

Definitions

  • the present invention relates to a centrifugal separator according to the preamble of claim 1 and a method for controlling a radial level of an interface layer in a centrifugal separator according to the preamble of claim 6.
  • a centrifugal separator according to the preamble of claim 1 and a method for controlling a radial level of an interface layer in a centrifugal separator according to the preamble of claim 6 are known from WO 00/37177 A1 , which describes control equipment for a centrifugal separator for separating a light liquid of relatively low density and a heavy liquid of relatively high density from a mixture containing these two liquids.
  • the liquids may, for instance, be oil and water.
  • the control equipment is intended for a centrifugal separator comprising a rotor, which is rotatable around a rotational axis and forms an inlet for said mixture and a separating chamber, which communicates with the inlet and which has a radially inner zone and a radially outer zone, said zones being adapted during a separating operation to contain separated light liquid and separated heavy liquid respectively.
  • a centrifugal separator of this kind may have outlets configured in several different ways for the separated liquids.
  • the rotor may be provided with so-called overflow outlets for both of the liquids or an overflow outlet for one liquid and another kind of outlet for the other liquid.
  • An outlet of such other kind may be constituted by, for instance, a non-rotatable so-called paring member or by nozzles situated in the surrounding wall of the rotor. Nozzles are used as a rule where the mixture supplied contains not only said two liquids but also a relatively large amount of solids which are heavier than the two liquids.
  • the separated solids together with part of the separated heavy liquid may thus be discharged through the nozzles situated at the periphery of the rotor, whereas the separated light liquid is removed from a central part of the rotor via an overflow outlet or a paring member.
  • the rotor may also form a space which communicates with the radially outer zone of the separating chamber in such a way that during a separating operation it will contain separated heavy liquid (but not separated light liquid). An excess of separated heavy liquid which does not leave the separating chamber via said nozzles can therefore be removed from the rotor via this space.
  • centrifugal separator in which solids as well as two different liquids can be separated is a so-called decanter centrifuge.
  • a centrifugal separator of this kind there is in the rotor a so-called sludge conveyor, which is adapted to transport separated solids along the surrounding wall of the rotor to a sludge outlet.
  • the sludge outlet is often situated at a level in the rotor which is radially within the level of the outlets for the two separated liquids.
  • a particular separating operation in which this has caused problems is the removal of sand and water from oil in connection with oil recovery from so-called oil sands.
  • nozzle centrifuges are used in at least two separating steps.
  • a mixture of oil, water, solvent and sand residues is introduced into a nozzle centrifuge and, in addition to the mixture, an amount of water is supplied to the centrifuge.
  • the water supplied is added to ensure that the interface layer formed, in the rotor's separating chamber, between oil and water shall not be displaced radially outwards. Such a radial displacement of the interface layer might otherwise take place after a number of hours of operation because of said nozzles becoming worn by the outflowing sand and therefore releasing more water per unit of time than at the beginning of the separating operation.
  • the oil still contains not only solvent but also residues of sand and water. This oil is conducted out from a central part of the rotor via a paring member and is pumped on to another nozzle centrifuge to undergo a second separating step.
  • Said control equipment includes a pressure vessel for water, the lower part of which communicates via a conduit with a liquid transfer member, situated in said space in the rotor of the centrifugal separator, for the introduction of water into or discharge of water from the rotor.
  • a gas pressure is maintained (usually by means of nitrogen gas) and its magnitude is continuously controlled on the basis of the amount of water present at the time in the pressure vessel, so that the liquid pressure at the bottom of the pressure vessel, and therefore in the conduit via which the pressure vessel communicates with said space in the centrifugal rotor, is always kept constant at a predetermined value.
  • This constant value of the liquid pressure in said conduit corresponds to a desired radial level in the separating chamber of the rotor for the interface layer therein formed between separated oil and separated water. If the interface layer moves radially outwards from the desired level, the pressure drops in said space in the rotor, with the result that water is pushed from the pressure vessel into the rotor via the conduit until the interface layer returns to the desired radial level.
  • a level-detecting member in the pressure vessel is adapted to initiate when necessary a supply of new water to the pressure vessel so that it never becomes empty of water.
  • WO 00/37177 A1 said control equipment is expensive, complicated and bulky. Therefore WO 00/37177 A1 describes a less expensive and a more simple control equipment for a centrifugal separator of the kind described above.
  • That control equipment includes a device for supply of a control liquid which is of higher density than said light liquid.
  • the supply device has a pressure source for delivering pressurised control liquid, and a supply conduit which at its one end is connected to the pressure source in order to receive pressurised control liquid and at its other end is connected to a liquid transfer member in order to introduce pressurised control liquid into the rotor.
  • the supply device is adapted upon need to supply control liquid to the rotor in only such amount per unit of time as is required to prevent an interface layer formed in the separating chamber between separated light liquid on the one hand and separated heavy liquid or control liquid on the other hand from moving radially outwards from a predetermined radial supply level.
  • the control equipment also includes a device for discharge of separated heavy liquid and/or control liquid from said space in the rotor.
  • the discharge device has a discharge conduit which is adapted, when the rotor is supplied with an excess of heavy liquid, to discharge separated heavy liquid and/or control liquid from the rotor through said discharge conduit in such amount per unit of time as is required to prevent said interface layer from moving radially inwards from a predetermined radial discharge level.
  • the control equipment described in WO 00/37177 A1 is characterised in that the discharge device is arranged to discharge liquid from said space in the rotor a different way than through said supply device.
  • This control equipment differs from the control equipment previously described in that the pressure source in the supply device is not integrated in the discharge device, i.e. the control equipment has respective separate conduits for supply and discharge of liquid.
  • the separated heavy liquid and/or control liquid leaving the rotor therefore need not be accumulated at an elevated pressure and no pressure vessel is needed. Consequently, there is also no need for a system for compression of gas and for control of the pressure of such gas.
  • the pressure source may be constituted by a simple liquid pump and the whole control of the supply of control liquid and discharge of separated heavy liquid and/or control liquid may be by means of so-called constant pressure valves. Any container needed for a buffer amount of control liquid may be free of pressure and common to several centrifugal separators.
  • the equipment includes a double set of components in the form of respective separate supply and discharge conduits with constant pressure valves. There is therefore a need to further simplify the control equipment for the centrifugal separator.
  • An object of the present invention is to provide a centrifugal separator and a method of the initially described kind which comprise simple, inexpensive and compact control equipment.
  • centrifugal separator which is characterised in that the pressure source is a variable speed pump, wherein said means for detecting the interface layer level is arranged to communicate with means for controlling the speed of the pump in such a way that the supply and discharge respectively of the liquid in said space take place in such amount per unit of time that the interface layer in the separating chamber is within said predetermined inner and outer radial levels.
  • control liquid used may for example be the heavy liquid (water).
  • the invention therefore does not require the control liquid to be in some form other than the heavy liquid, although that is also possible. All that is required is that the control liquid be of higher density than the light liquid.
  • the object is also achieved by the method initially described which is characterised in that the liquid is supplied to and discharged from said space by means of a variable speed pump as said pressure source, the speed of the pump being controlled, by the interface layer level detected in the separating chamber, in such a way that the supply and discharge respectively take place in such amount per unit of time that said interface layer in the separating chamber is within said predetermined inner and outer radial levels.
  • the invention differs from the first of the previously described known forms of control equipment in that the separated heavy liquid and/or control liquid need not be accumulated at an elevated pressure, i.e. there is no need for any pressure vessel with systems for compression of gas and control of the pressure of such gas.
  • the invention differs from the second of the previously described known forms of control equipment in that neither the separate discharge conduit nor said constant pressure valves are necessary.
  • supply and discharge of control liquid take place via the same conduit.
  • the conduit with the variable speed pump is thus adapted to allow liquid flow in both directions, i.e. in both a supply and a discharge direction through the pump.
  • the speed control of the pump eliminates the need for said constant pressure valves, since the speed control is itself adapted to control the liquid pressure in said conduit in such a way that the amount of control liquid supplied and discharged respectively per unit of time is such that said interface layer is within said predetermined interface layer levels.
  • a further object of the present invention is to provide a centrifugal separator with control equipment which in a simple and effective way controls said level of the interface layer in the separating chamber.
  • a further object of the present invention is to provide a centrifugal separator with control equipment which in a simple and effective way detects the interface layer level in the separating chamber.
  • a further object of the present invention is to provide a centrifugal separator with control equipment which in a simple and effective way controls the pump for delivery of pressurised control liquid.
  • the pump is a reversible pump. Reversing the pump makes it possible for the liquid to be also pumped from the space in the discharge direction, thereby achieving quicker control when the level of the interface layer is within the inner predetermined radial level. It should be noted, however, that the pump need not be reversible for discharge of control liquid.
  • the pump may for example be a variable speed rotary pump, e.g. a centrifugal pump, adapted to allow backflow of liquid.
  • the level of the interface layer in the separating chamber depends on the speed of the pump, wherein a lowering of the speed of the pump (or having the pump at standstill) will cause the interface layer to move radially outwards as a result of the liquid pressure from the separating chamber overcoming the counterpressure from the pump, thus discharging the liquid from said space.
  • said means for controlling the pump comprises a frequency converter.
  • the frequency converter makes it possible for the speed of the pump to be controlled in an energy-efficient and simple way.
  • said means for detecting the interface layer level in the separating chamber comprises a pressure sensor arranged to detect a change in the liquid pressure in the space, which liquid pressure depends on the level of the free liquid surface in the space.
  • the level of the interface layer in the separating chamber will affect the free liquid surface in the space. If the interface layer moves radially outwards, the free liquid surface in the space will also move radially outwards, and vice versa. If the free liquid surface in the space moves radially outwards, the liquid pressure in the space will drop (at a given radial level).
  • a device may be provided for detecting the radial position of the free liquid surface in the space.
  • a detection operation of this kind refers to detecting the radial position of the interface layer formed in the separating chamber.
  • said conduit is in liquid pressure transmitting communication with the space via the liquid transfer member, and the pressure sensor is arranged to detect a change in the liquid pressure in the conduit between the pump and the liquid transfer member.
  • the liquid pressure in the conduit provides a measure of the radial level of the free liquid surface in the space.
  • Fig. 1 discloses schematically a longitudinal section through a rotor which forms part of a centrifugal separator, and control equipment according to the invention.
  • Figure 1 discloses, in an example of an embodiment of the invention, a centrifugal separator which comprises a rotor having a lower part 1 and an upper part 2, which parts are connected to one another by means of a locking ring 3.
  • the rotor is situated uppermost on a vertical driveshaft 4 which is connected to the lower rotor part 1 and rotatable around a rotational axis R.
  • a distributor 5 which divides the rotor interior into a central inlet chamber 6 and an annular separating chamber 7 extending around the distributor.
  • the distributor 5 rests on a central portion of the lower rotor part 1 via radially and axially extending wings (not shown) which are distributed around the rotational axis R of the rotor.
  • the inlet chamber 6 communicates with the separating chamber 7 via channels 8 situated between said wings.
  • a stationary inlet pipe 9 extends from above axially into the rotor and opens in the inlet chamber 6.
  • a stack of conical separating discs 10 is kept axially in place between the upper part 2 of the rotor and the lower part of the distributor 5.
  • Each separating disc 10 like the lower part of the distributor, has at its outer periphery a number of recesses 11 distributed around the rotational axis R and situated axially in line with one another.
  • the embodiment disclosed comprises separating discs and a distributor with recesses at its outer peripheral edge
  • rotors also exist which exhibit separating discs with a distributor which has recesses or holes radially within its outer peripheral edge (i.e. holes a short distance in on the conical surface of the separating disc), which recesses or holes are likewise distributed around the rotational axis R and situated axially in line with one another.
  • the lower rotor part 1 carries several nozzles 12 distributed around the rotational axis R of the rotor.
  • Each nozzle 12 has a through channel via which liquid and finely divided solids can be ejected from the separating chamber 7.
  • the upper rotor part 2 carries a central annular cap 13, which on its inside delimits an annular outlet chamber 14 open radially inwardly towards the rotational axis of the rotor.
  • the outside of the stationary inlet pipe 9 supports an outlet member 15 in the form of a paring disc which extends radially outwards into the outlet chamber 14.
  • a radially inner zone 7a of the separating chamber 7 communicates with the outlet chamber 14 via an overflow outlet 16 formed by an annular flange which is supported by, and situated on the inside of, the upper rotor part 2.
  • the overflow outlet 16 is not necessary for the function of the rotor and might, if desired, be dispensed with. Alternatively, the outlet member 15 might be dispensed with, in which case liquid flowing out from the separating chamber 7 might leave the rotor directly.
  • An annular space 17 delimited in the lower part 1 of the rotor is open radially inwardly towards the rotational axis R of the rotor.
  • the space 17 communicates with a radially outer zone 7b of the separating chamber 7 via channels 18 and 19 and a plurality of pipes 20 distributed around the rotational axis R.
  • the rotor may of course be provided with other means for creating said connection between the radially outer zone 7b and the annular space 17.
  • the rotor may be provided with channels integrated in the lower part 1 of the rotor, in which case the channels will constitute extensions of the channels 18 and 19.
  • the pipes 20 may be replaced by a separate plate arranged at the lower part 1 of the rotor and provided with channels which connect to the channels 18 and 19 of the rotor part and which create said connection between the radially outer zone 7b and the annular space 17.
  • a stationary liquid transfer member 21 extends into the space 17 and is adapted to conduct liquid into the space 17 or conduct liquid out therefrom.
  • a vertical broken line 22 in the separating chamber 7 represents a certain radial level therein.
  • the centrifugal rotor is suitable for treating a mixture of oil and water and of solids therein suspended.
  • the mixture is supplied to the rotor via the inlet pipe 9 and is forwarded from the inlet chamber 6 to the separating chamber 7 via the channels 8.
  • the mixture is distributed, via distribution channels formed by the recesses 11 in the separating discs, to the various interspaces between the separating discs 10, in which the various mixture components are separated from one another. Separated oil flows radially inwards and further out from the rotor via the outlet chamber 14 and the outlet member 15, whereas separated solids and water leave the rotor via the nozzles 12.
  • the radial position of the radial level 22 shown in the figure need not be the state of equilibrium formed in practice, nor the desired predetermined radial level.
  • the desired predetermined radial level may be somewhat elsewhere in the separating chamber (e.g. at or somewhat radially outside the distribution channels formed by the recesses 11 in the separating discs). It is further presumed that separated solids leave the rotor via the nozzles 12 without blocking them for outflowing separated water.
  • Control equipment of this kind is connected to the liquid transfer member 21 and is adapted either to supply via the latter to the rotor a variable amount of control liquid (e.g. water) if said interface layer in the rotor tends to move radially outwardly from the level 22, or to remove a variable amount of water from the rotor if the interface layer tends to move radially inwardly from the level 22.
  • control liquid e.g. water
  • the control equipment comprises a device which has a pressure source in the form of a variable speed pump 23 and a conduit 24 which is connected at its one end to the pump 23 and at its other end to the liquid transfer member 21.
  • the pump 23 is connected to a so-called VFD (variable frequency drive), i.e. a frequency converter 25 for controlling the speed of the pump 23, which frequency converter 25 communicates with a sensor 26 in the form of a pressure sensor P adapted to detect a change in the liquid pressure in the conduit between the pump 23 and the liquid transfer member 21.
  • VFD variable frequency drive
  • the liquid transfer member 21 may within the scope of the invention be of various kinds. If it is stationary, i.e. non-rotating, as illustrated in the figure, it may with advantage comprise an annular disc surrounding the rotor's rotational axis R and extending into the space 17.
  • the liquid transfer member may form one or more radially extending channels, or form one or more annular channels extending around the rotational axis R (see SE 76670 ). In either case the channels lead into the liquid which is present in the space 17. Rotation of the rotor causes a liquid pressure, the magnitude of which depends on the position of the free liquid surface of the liquid body which rotates together with the rotor in the space 17.
  • the position of the liquid surface in the space 17 is itself influenced by any movement of the radial position 22 of the interface layer in the separating chamber 7 between separated oil and separated water.
  • the free liquid surface in the space 17 also moves radially outwards, whereupon the pressure in the conduit 24 drops.
  • the pressure in the conduit 24 rises.
  • the speed of the pump 23 increases to raise the pressure in the conduit 24 and pump water into the space 17 and further via the channels 18, 19 and the pipes 20 to the separating chamber 7.
  • the speed increase will be greater or lesser depending on how low the pressure in the conduit 24 drops, and the amount of water pumped in per unit of time will be such that the interface layer between oil and water in the separating chamber is kept radially within said outer predetermined radial level.
  • the speed reduction will be greater or lesser (or the pump may even be reversed) depending on how much the pressure in the conduit 24 increases, wherein the amount of water discharged (or pumped) per unit of time will be such that the interface layer between oil and water in the separating chamber 7 is kept radially outside said inner predetermined radial level.
  • the control equipment may also comprise a container 27 for control liquid (water) which is maintained in a desired quantity and at a desired temperature.
  • the container 27 is provided with an inlet conduit, an outlet conduit, a float, valves controlled by the float, and a warming device (not shown in Fig. 1 ).
  • a container is known per se from WO 00/37177 A1 (see Fig. 6).
  • the pump 23 is arranged to use the container 27 as a control liquid reservoir in such a way that control liquid is both supplied to and discharged from the container 27 upon adjustment of the interface layer level 22 in the separating chamber 7. Control liquid supplied to the container 27 may thus be reused.
  • Any suitable pump desired may be used for the transport of water from and to the space 17, subject to the pump being adapted to allow flow in both directions.
  • Such pumps are well known to one skilled in the art and are therefore not described here.
  • the pressure sensor 26 for detecting the pressure in the conduit may be replaced by other means for detecting the level of the interface layer.
  • means may be provided for detecting the radial position of the free liquid surface in the space 17.
  • other indirect means of detecting the interface layer level which detect at least one parameter related to the position of the interface layer and which, on the basis of said parameter or parameters, calculate or otherwise determine the radial position of the interface layer.
  • a detection operation of this kind refers to detecting the radial position of the interface layer formed between oil and water in the separating chamber 7. If so desired, it is of course also possible to provide means for direct detection of the radial position of the interface layer.
  • Control equipment according to the invention will of course also work in conjunction with a hermetically closed centrifugal rotor, i.e. a centrifugal rotor in which a space 17 is intended to be completely filled with liquid and to communicate with the interior of a stationary liquid transfer member which seals against the rotatable centrifugal rotor.
  • a hermetically closed centrifugal rotor i.e. a centrifugal rotor in which a space 17 is intended to be completely filled with liquid and to communicate with the interior of a stationary liquid transfer member which seals against the rotatable centrifugal rotor.

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  • Centrifugal Separators (AREA)
EP10714387.7A 2009-02-24 2010-02-18 Centrifugal separator and method for separating Active EP2401087B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE0950101A SE533360C2 (sv) 2009-02-24 2009-02-24 Centrifugalseparator och metod för separering
PCT/SE2010/050186 WO2010098714A1 (en) 2009-02-24 2010-02-18 Centrifugal separator and method for separating

Publications (2)

Publication Number Publication Date
EP2401087A1 EP2401087A1 (en) 2012-01-04
EP2401087B1 true EP2401087B1 (en) 2013-06-19

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Application Number Title Priority Date Filing Date
EP10714387.7A Active EP2401087B1 (en) 2009-02-24 2010-02-18 Centrifugal separator and method for separating

Country Status (7)

Country Link
EP (1) EP2401087B1 (ru)
CN (1) CN102413940B (ru)
BR (1) BRPI1008001B1 (ru)
CA (1) CA2753349C (ru)
RU (1) RU2480291C1 (ru)
SE (1) SE533360C2 (ru)
WO (1) WO2010098714A1 (ru)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2366457B1 (en) * 2010-03-19 2013-03-06 Alfa Laval Corporate AB Device and method for monitoring and adjusting the radial position of an interface layer in a centrifugal separator
DE102013111586A1 (de) * 2013-10-21 2015-04-23 Gea Mechanical Equipment Gmbh Verfahren zur kontinuierlichen Klärung einer fließfähigen Suspension mit schwankendem Feststoffgehalt mit einer Zentrifuge, insbesondere einem selbstentleerenden Separator
US9400196B2 (en) * 2013-11-12 2016-07-26 Syncrude Canada Ltd. Method of detecting and controlling E-line loss in a centrifuge
DE102014116404A1 (de) * 2014-11-11 2016-05-12 Gea Mechanical Equipment Gmbh Verfahren zum Überwachen und/oder Regeln des Betriebs einer Zentrifuge

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2926237C2 (de) * 1979-06-29 1981-07-02 Westfalia Separator Ag, 4740 Oelde Selbstentleerende Klärtrommel
SE440487B (sv) * 1983-12-21 1985-08-05 Alfa Laval Marine Power Eng Anordning vid centrifugalseparator
DE3601814A1 (de) * 1986-01-22 1987-07-23 Westfalia Separator Ag Verfahren und vorrichtung zum trennen von zwei fluessigen phasen mittels einer zentrifuge
SU1597221A1 (ru) * 1988-04-29 1990-10-07 Всесоюзный Научно-Исследовательский И Экспериментально-Конструкторский Институт Продовольственного Машиностроения Барабан центробежного сепаратора
SE510541C2 (sv) * 1997-09-29 1999-05-31 Alfa Laval Ab Regleranordning för centrifugalseparator
SE514774C2 (sv) * 1998-12-21 2001-04-23 Alfa Laval Ab Reglerutrustning för centrifugalseparator samt sätt att reglera en separeringsoperation
SE529562C2 (sv) * 2006-02-13 2007-09-18 Alfa Laval Corp Ab Sätt att övervaka centrifugalseparator
US20080041772A1 (en) * 2006-08-17 2008-02-21 Gambro Bct, Inc. Blood Processing Apparatus with Robust Outflow Process Control

Also Published As

Publication number Publication date
RU2480291C1 (ru) 2013-04-27
WO2010098714A1 (en) 2010-09-02
CN102413940A (zh) 2012-04-11
CA2753349A1 (en) 2010-09-02
CN102413940B (zh) 2013-12-18
SE0950101A1 (sv) 2010-08-25
EP2401087A1 (en) 2012-01-04
CA2753349C (en) 2014-04-08
BRPI1008001B1 (pt) 2020-03-03
SE533360C2 (sv) 2010-09-07
BRPI1008001A2 (pt) 2016-02-23

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