EP3700678A1 - Method for processing a flowable product and centrifuge - Google Patents
Method for processing a flowable product and centrifugeInfo
- Publication number
- EP3700678A1 EP3700678A1 EP18795413.6A EP18795413A EP3700678A1 EP 3700678 A1 EP3700678 A1 EP 3700678A1 EP 18795413 A EP18795413 A EP 18795413A EP 3700678 A1 EP3700678 A1 EP 3700678A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- centrifuge
- product
- plate package
- package
- particles
- 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.)
- Granted
Links
- 230000009969 flowable effect Effects 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000012545 processing Methods 0.000 title claims abstract description 9
- 239000002245 particle Substances 0.000 claims abstract description 45
- 239000007787 solid Substances 0.000 claims abstract description 19
- 239000007791 liquid phase Substances 0.000 claims abstract description 14
- 239000007790 solid phase Substances 0.000 claims abstract description 9
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 239000012811 non-conductive material Substances 0.000 claims description 12
- 230000008021 deposition Effects 0.000 claims description 9
- 230000005684 electric field Effects 0.000 claims description 5
- 238000007600 charging Methods 0.000 claims description 3
- 238000005352 clarification Methods 0.000 claims description 3
- 239000012071 phase Substances 0.000 claims description 3
- 238000005191 phase separation Methods 0.000 claims description 2
- 238000010276 construction Methods 0.000 claims 1
- 238000000151 deposition Methods 0.000 abstract description 10
- 238000000926 separation method Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 238000013461 design Methods 0.000 description 4
- 238000007786 electrostatic charging Methods 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011554 ferrofluid Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/10—Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C5/00—Separating dispersed particles from liquids by electrostatic effect
-
- 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
- B04B11/00—Feeding, charging, or discharging bowls
- B04B11/02—Continuous feeding or discharging; Control arrangements therefor
Definitions
- the invention relates to a method for processing a flowable product according to the preamble of claim 1 and a centrifuge, in particular a separator, according to the preamble of claim 9.
- DE 10 2006 022 156 A1 discloses a method and a device for the treatment of liquids, in which an incoming flowable product is separated in a centrifuge into two liquid phases and a solid phase.
- the product for example a contaminated lubricating oil
- the product is separated into two partial streams, which are conducted past a positive or a negative electrode.
- the particles which are contained in the first partial flow are positively charged and the particles of the second partial flow are negatively charged.
- both partial streams are combined in a collection tank, whereby the positively charged particles and the negatively charged particles conglomerate to form larger particle dressings due to the mutual electrostatic attraction. These conglomerates are then easier to separate from the liquid in the centrifugal field.
- SU 5 51 036 discloses a centrifuge which enables electrostatic charging of particles within a non-continuous centrifuge.
- an electrode is arranged in an inlet chamber on the axis of rotation of the centrifuge. After electrostatic charging of the particles, they are passed on to a drum space in which the particles are deposited in solid collecting pockets. The clarified liquid is then removed from the centrifuge. The solid collecting pockets are embedded in the wall of the centrifuge.
- continuous operation is not possible with this centrifuge because the collection bags must be emptied at regular intervals.
- the invention achieves this object by a method having the features of claim 1 and a centrifuge having the features of claim 8.
- a method for processing a flowable product with a centrifuge in particular a separator with a vertical axis of rotation, with a rotatable centrifuge drum in which a plate package, at least one product outlet and at least one solids discharge opening is arranged, comprises the following steps:
- the electric field between the plates of the plate package and the remaining part of the centrifuge insulated therefrom is generated by impressing a charge starting from a DC voltage source.
- step a) the transmission of the positive or negative charge from the outside to a component of the centrifuge can take place, wherein one pole of the DC voltage source Le is contacted with an outer wall of this component and this component consists of electrically conductive material. After charge transfer, this charge is transferred or transferred to the plate package of the centrifuge.
- the pretreatment of step a) is preferably carried out outside the drum. The pretreatment is also preferably carried out in such a way that the particles are attracted to the charge of the plate package.
- the pretreatment in step a) can take place according to a first advantageous variant of the invention by an electrostatic charging of the particles, for example outside the centrifuge.
- the product to be processed is passed past a positively or negatively charged electrode, whereby particles, for example solid particles, are charged to the electrode prior to entry into the centrifuge.
- This electrode is preferably arranged outside the drum. It is also conceivable, however, to integrate them into the inlet of the drum.
- the pretreatment in step a) can be carried out according to an alternative variant of the invention but also by adding a ferrofluid, in order to achieve the above-mentioned effect.
- step d After the particles have been deposited in step d), it is advantageously possible for the electric field to be switched off and / or discharged on the disk package, so that the deposited particles more easily slip off the surface of the disk into the solids.
- the deposition can be monitored, for example by a probe on a product outlet of the liquid phase or liquid phase. If the proportion of solids exceeds a predetermined value, the deposition on the plate is insufficient. By monitoring the deposition, the process can be adapted to the respective product. Alternatively, the feed can be closed during the polarity reversal or switching off of the electric field.
- a centrifuge in particular a separator, a centrifuge drum, in particular a continuously operable separator drum with a vertical axis of rotation, in which a disc package is arranged, wherein the centrifuge drum at least one product feed for supplying a product to be processed, a disc pack for phase separation and at least an outlet for draining a liquid phase and a drain for discharging at least one further phase, in particular a liquid phase or a solid phase.
- the centrifuge also has at least one means for generating an electric charge on the plates of the plate package or in plate columns of the plate package.
- particles are deposited in the region of a centrifuge, at which the deposition usually takes place without the additional influence of electrostatics.
- the deposition rate of these charged particles is improved, and crossing of the already deposited particles with the product feed stream is prevented.
- a suitable DC voltage source can be used, wherein the height of the generated voltage is preferably adjustable.
- a positive pole is present at one point of the separator and a negative pole at another point of the separator.
- One of the poles is conductively connected to the plate package.
- the disk pack is electrically insulated from the outer wall of the centrifuge drum by a coating or other non-conductive material, so that it can not come to a short circuit due to contact of the two components.
- a suitable voltage level for such a DC voltage source is in the range between 5000 and 20,000 volts.
- the means for generating an electric charge on the plates of the plate package is preferably arranged outside the centrifuge drum.
- a first pole of the DC voltage source can be arranged with positive or negative charge on the outer wall of a pump element of the centrifuge, which is connected to the plate package.
- the pole only has to be attached to the pump element, further design adjustments of the centrifuge drum are not necessary. This is advantageous, since thus an already existing centrifuge can still be retrofitted.
- FIG. 1 is a partial sectional view of a separator drum in a hermetically sealed design.
- a rotatable Separatortrommel 1 with vertical axis of rotation D is set to a rotary spindle 2, which is driven by a direct drive or by a belt drive, not shown here.
- the rotary spindle 2 is conically shaped along an upper circumferential region and fastened with a fastening means 6 on the drum base 20.
- a product inlet 4 is adjoined by a product inlet pipe 5 which rotates during operation and which is aligned concentrically with the axis of rotation D.
- the product P passes into a manifold 7 having manifold bores or fins from which the flowable product is e.g. can emerge in the radial direction in the interior of the separator drum 1. It is also conceivable (not shown here) to direct the product from the distributor into at least one rising channel in the plate package.
- the incoming product flows into the plate gap between conical plates of a plate package 1 1 spaced apart from one another by axially intermediate spacers.
- a better separation of solid particles in the disk columns of a Teller package is made possible in the present case by applying the plate package 1 1 with an electric charge. This also means that already deposited particles stick to the underside of the plate.
- an outer wall 1 8 of the separator drum 1 or an outer wall 1 9 of the pump element 1 2 via a respective electrical line 1 5a and 1 5b connected to a positive and a negative pole of a DC voltage source 14.
- Another component, such as the actual separator drum 1 is polarized in the opposite direction.
- the plate package 1 1 is insulated from the inner wall of the separator drum 1, here by one or more non-conductive material layers 1 6, 1 7 above and below the plate package 1 first
- the distributor 7 is also insulated by an upper material layer 1 7 and a lower material layer 21.
- drum base 20 may also be insulated from the rotary spindle 2 by an electrically non-conductive material layer 22.
- the product inlet pipe 5 and the manifold 7 are preferably made of an electrically non-conductive material or have a non-conductive coating, so that preferably already charged before entering the drum parts not settle or unload here already on the components.
- a pretreatment in the manner of step a) of claim 1. the product is first passed before entering the rotating separator drum to a negative or positive charged electrode of a DC voltage source, so that the solid particles in the product charge electrically.
- This electrode can also be arranged alternatively in the product feed 4 or in the feed pipe 5.
- the loading of the solid particles can also be done elsewhere before the entry of the product flow in the plate gap of the plate package 1 1.
- a suitable voltage level for such a DC voltage source is in the range between 5000 and 20,000 volts.
- the product supply pipe 5 and the distributor 7 consist of non-conductive material or are coated with non-conductive material, so that the deposition preferably takes place only in the disk package.
- the product After the product has entered the drum 1, it enters the plate column of the plate pack 1 1.
- the charge of the particles of the product is opposite to the charge of the plates, so that the plate exerts an electrostatic attraction on the charged particles, which collect increasingly on the plates.
- the plate column therefore continue to grow over time.
- the plate package increases with time. It is therefore advantageous if this is suitably monitored during operation (for example based on the inflow quantity or the outflow quantity) and if, depending on the monitoring or periodically at predetermined time intervals, the plate package is reversed and, if appropriate, the drum is emptied rinse out the attached particles.
- the DC voltage source is preferably on connected the control system of the centrifuge (not shown here).
- FIG. 1 shows a separator which allows a solid-liquid separation.
- the method can also be applied analogously to three-phase separators.
- the deposition of solids on a charged plate package in other designs, e.g. be used with hanging drums.
- the inventive method and the centrifuge are suitable for a wide variety of products, but in particular for the purification of a contaminated oil. It should also be noted that although the embodiment is preferred as a hermetically sealed machine with rotating inlet pipe and an instructive pump element, in which the product is pumped through the machine, it is not mandatory.
Landscapes
- Centrifugal Separators (AREA)
Abstract
Ein Verfahren zur Verarbeitung eines fließfähigen Produktes (P) mit einer Zentrifuge, insbesondere einem Separator, mit vertikaler Drehachse (D) mit einer drehbaren Zentrifugentrommel (1) in der ein Tellerpaket (11) angeordnet ist, zumindest einen Produktablauf (13) zum Austrag zumindest einer flüssigen Phase (LP) und zumindest einer Feststoffaustragsöffnung (10) zum Austrag einer Feststoffphase (SP), gekennzeichnet durch folgende Schritte a) Vorbehandeln des fließfähigen Produktes (P), so dass Teilchen in diesem Produkt verstärkt durch elektrisch aufgeladene Bauteile angezogen werden; a) Zuleiten des fließfähigen Produktes (P) zu dem Tellerpaket (11); b) Erzeugen einer elektrischen Ladung auf den Tellern des Tellerpakets (11) und c) Abscheiden der aufgeladenen Teilchen aus dem fließfähigen Produkt (P) innerhalb des Tellerpakets (11) unter Einfluss von elektrostatischen Anziehungskräften und eines Zentrifugalfeldes und eine Zentrifuge.A method for processing a flowable product (P) with a centrifuge, in particular a separator, with a vertical axis of rotation (D) with a rotatable centrifuge drum (1) in which a disc package (11) is arranged, at least one product outlet (13) for discharging at least a liquid phase (LP) and at least one solids discharge opening (10) for discharging a solid phase (SP), characterized by the following steps: a) pretreating the flowable product (P) so that particles in this product are increasingly attracted by electrically charged components; a) supplying the flowable product (P) to the plate package (11); b) generating an electric charge on the plates of the plate package (11) and c) depositing the charged particles from the flowable product (P) within the plate package (11) under the influence of electrostatic attraction forces and a centrifugal field and a centrifuge.
Description
Verfahren zur Verarbeitung eines fliessfähigen Produktes und Zentrifuge Process for processing a flowable product and centrifuge
Die Erfindung betrifft ein Verfahren zur Verarbeitung eines fließfähigen Produktes nach dem Oberbegriff des Anspruchs 1 und eine Zentrifuge, insbesondere einen Separator, nach dem Oberbegriff des Anspruchs 9. The invention relates to a method for processing a flowable product according to the preamble of claim 1 and a centrifuge, in particular a separator, according to the preamble of claim 9.
Die DE 10 2006 022 156 A1 offenbart ein Verfahren und eine Vorrichtung zur Aufbereitung von Flüssigkeiten, bei dem ein zulaufendes fließfähiges Produkt in einer Zentrifuge in zwei Flüssigphasen und eine Feststoffphase getrennt wird. Das Produkt, beispielsweise ein verunreinigtes Schmieröl, wird hierzu in zwei Teilströme getrennt, die an einer positiven bzw. einer negativen Elektrode vorbeigeleitet werden. Dabei werden die Partikel, welche in dem ersten Teilstrom enthalten sind, positiv aufgeladen und die Partikel des zweiten Teilstromes negativ aufgeladen. Vor dem Einleiten der Flüssigkeit in die Zentrifuge werden beide Teilströme in einem Sammeltank vereinigt, wobei die positiv geladenen Partikel und die negativ geladenen Partikel aufgrund der gegenseitigen elektrostatischen Anziehung zu größeren Partikelverbänden konglomerieren. Diese Konglomerate sind anschließend im Zentrifugalfeld leichter aus der Flüssigkeit abzutrennen. Die SU 5 51 036 offenbart eine Zentrifuge, die ein elektrostatisches Aufladen von Partikeln innerhalb einer nicht kontinuierlich arbeitenden Zentrifuge ermöglicht. Hierfür ist eine Elektrode in einer Zulaufkammer auf der Drehachse der Zentrifuge angeordnet. Nach der elektrostatischen Aufladung der Partikel werden diese in einen Trommelraum weitergeleitet, in welchem die Partikel in Feststoffsammeltaschen abgeschieden werden. Die geklärte Flüssigkeit wird anschließend aus der Zentrifuge abgeführt. Die Feststoffsammeltaschen sind in der Wandung der Zentrifuge eingelassen. Anders als bei einer üblichen Zentrifuge mit einem Tellerpaket ist bei dieser Zentrifuge allerdings kein kontinuierlicher Betrieb möglich, da die Sammeltaschen in regelmäßigen Abständen ent- leert werden müssen. DE 10 2006 022 156 A1 discloses a method and a device for the treatment of liquids, in which an incoming flowable product is separated in a centrifuge into two liquid phases and a solid phase. For this purpose, the product, for example a contaminated lubricating oil, is separated into two partial streams, which are conducted past a positive or a negative electrode. In this case, the particles which are contained in the first partial flow are positively charged and the particles of the second partial flow are negatively charged. Before introducing the liquid into the centrifuge, both partial streams are combined in a collection tank, whereby the positively charged particles and the negatively charged particles conglomerate to form larger particle dressings due to the mutual electrostatic attraction. These conglomerates are then easier to separate from the liquid in the centrifugal field. SU 5 51 036 discloses a centrifuge which enables electrostatic charging of particles within a non-continuous centrifuge. For this purpose, an electrode is arranged in an inlet chamber on the axis of rotation of the centrifuge. After electrostatic charging of the particles, they are passed on to a drum space in which the particles are deposited in solid collecting pockets. The clarified liquid is then removed from the centrifuge. The solid collecting pockets are embedded in the wall of the centrifuge. However, unlike a conventional centrifuge with a disc pack, continuous operation is not possible with this centrifuge because the collection bags must be emptied at regular intervals.
Es ist die Aufgabe der vorliegenden Erfindung, ausgehend vom Stand der Technik, ein Verfahren zur Verarbeitung eines fließfähigen Produktes zu schaffen und eine Zentrifuge bereitzustellen, welche einen alternativen Lösungsweg für eine bessere Abscheidung von Teilchen ermöglicht. Die Erfindung löst diese Aufgabe durch ein Verfahren mit den Merkmalen des Anspruchs 1 und eine Zentrifuge mit den Merkmalen des Anspruchs 8. It is the object of the present invention, starting from the state of the art, to provide a method for processing a flowable product and to provide a centrifuge which allows an alternative approach for a better separation of particles. The invention achieves this object by a method having the features of claim 1 and a centrifuge having the features of claim 8.
Erfindungsgemäß weist ein Verfahren zur Verarbeitung eines fließfähigen Produktes mit einer Zentrifuge, insbesondere einem Separator mit vertikaler Drehachse, mit einer drehbaren Zentrifugentrommel in der ein Tellerpaket, zumindest ein Produktablauf und zumindest eine Feststoff austragsöffnung angeordnet ist, folgende Schritte auf: According to the invention, a method for processing a flowable product with a centrifuge, in particular a separator with a vertical axis of rotation, with a rotatable centrifuge drum in which a plate package, at least one product outlet and at least one solids discharge opening is arranged, comprises the following steps:
a) Vorbehandeln des fließfähigen Produktes, so dass Teilchen in diesem Produkt verstärkt durch elektrisch aufgeladene Bauteile angezogen werden; a) pretreatment of the flowable product so that particles in this product are increasingly attracted by electrically charged components;
b) Zuleiten des fließfähigen Produktes zu dem Tellerpaket; b) supplying the flowable product to the disk pack;
c) Erzeugen einer elektrischen Ladung auf den Tellern des Tellerpakets und c) generating an electric charge on the plates of the plate package and
d) Abscheiden der aufgeladenen Teilchen aus dem fließfähigen Produkt innerhalb des Tellerpakets (und somit unter Einfluss von elektrostatischen Anziehungskräften und eines Zentrifugalfeldes). d) depositing the charged particles from the flowable product within the plate package (and thus under the influence of electrostatic attractive forces and a centrifugal field).
Durch den gezielten Einsatz elektrostatischer Kräfte in den Tellerspalten im Zentrifugalfeld einer Zentrifuge wird auf einfache Weise ein besseres Abscheideverhalten von Teilchen an den Tellern des Tellerpakets erreicht. Zudem bleiben die bereits abgeschiedenen Teilchen an der Tellerunterseite haften, so dass ein Kreuzen vom Teilchen- und vom Produktzulaufstrom am Telleraußendurchmesser verhindert wird und damit auch, dass bereits abgeschiedene Teilchen ein zweites (oder drittes, ...) Mal in das Tellerpaket gelangen können. Through the targeted use of electrostatic forces in the disk gaps in the centrifugal field of a centrifuge, a better separation behavior of particles on the plates of the disk package is achieved in a simple manner. In addition, the already deposited particles remain adhered to the underside of the plate, so that a crossing of the particle and the product feed stream is prevented at the Telleraußendurchmesser and thus also that already deposited particles a second (or third, ...) times can get into the disk package.
Vorteilhafte Ausgestaltungen des erfindungsgemäßen Verfahrens sind der Gegenstand der Unteransprüche. Advantageous embodiments of the method according to the invention are the subject of the dependent claims.
Um die Wirkung der elektrischen geladenen Teller auf die geladenen Teilchen über einen großen Bereich zu ermöglichen, ist es von Vorteil, wenn diese auf den Tellern des Tellerpakets durch eine Flächenladung erzeugt wird. In order to enable the action of the charged electric particles over a wide range, it is advantageous if they are generated on the plates of the plate package by a surface charge.
Besonders bevorzugt wird das elektrische Feld zwischen den Tellern des Tellerpakets und dem hiervon isolierten restlichen Teil der Zentrifuge durch Aufprägen einer Ladung ausgehend von einer Gleichspannungsquelle erzeugt. Particularly preferably, the electric field between the plates of the plate package and the remaining part of the centrifuge insulated therefrom is generated by impressing a charge starting from a DC voltage source.
Dabei kann die Übertragung der positiven oder negativen Ladung von außen an ein Bauteil der Zentrifuge erfolgen, wobei ein Pol der Gleichspannungsquel- le mit einer Außenwandung dieses Bauteils kontaktiert ist und dieses Bauteil aus elektrisch leitendem Material besteht. Nach der Ladungsübertragung wird diese Ladung auf das Tellerpaket der Zentrifuge weitergeleitet bzw. übertragen. Das Vorbehandeln des Schrittes a) erfolgt vorzugsweise außerhalb der Trommel. Das Vorbehandeln erfolgt zudem vorzugsweie in einer Weise, dass die Teilchen von der Ladung des Tellerpakets angezogen werden. In this case, the transmission of the positive or negative charge from the outside to a component of the centrifuge can take place, wherein one pole of the DC voltage source Le is contacted with an outer wall of this component and this component consists of electrically conductive material. After charge transfer, this charge is transferred or transferred to the plate package of the centrifuge. The pretreatment of step a) is preferably carried out outside the drum. The pretreatment is also preferably carried out in such a way that the particles are attracted to the charge of the plate package.
Das Vorbehandeln in Schritt a) kann nach einer ersten vorteilhaften Variante der Erfindung durch ein elektrostatisches Aufladen der Teilchen erfolgen, beispielsweise außerhalb der Zentrifuge. Dabei wird das zu verarbeitende Produkt an einer positiv oder negativ geladenen Elektrode vorbeigeführt, wobei Teilchen, beispielsweise Feststoffteilchen, an der Elektrode vor dem Eintritt in die Zentrifuge aufgeladen werden. Diese Elektrode ist vorzugsweise außerhalb der Trommel angeordnet. Denkbar ist es aber auch, sie in den Zulauf der Trommel zu integrieren. The pretreatment in step a) can take place according to a first advantageous variant of the invention by an electrostatic charging of the particles, for example outside the centrifuge. In this case, the product to be processed is passed past a positively or negatively charged electrode, whereby particles, for example solid particles, are charged to the electrode prior to entry into the centrifuge. This electrode is preferably arranged outside the drum. It is also conceivable, however, to integrate them into the inlet of the drum.
Während des Abscheidens werden diese aufgeladenen Teilchen von den elektrostatisch aufgeladenen Tellern verstärkt in Richtung der Telleroberfläche ge- zogen, wo sie sich abscheiden und dann haften bleiben. During deposition, these charged particles are increasingly attracted to the plate surface by the electrostatically charged plates, where they deposit and then adhere.
Das Vorbehandeln in Schritt a) kann nach einer alternativen Variante der Erfindung aber auch durch Zugabe eines Ferrofluides erfolgen, um derart den vorstehend genannten Effekt zu erreichen. The pretreatment in step a) can be carried out according to an alternative variant of the invention but also by adding a ferrofluid, in order to achieve the above-mentioned effect.
Nach dem Abscheiden der Teilchen in Schritt d) kann vorteilhaft ein Ausschalten und/oder Entladen des elektrischen Feldes am Tellerpaket erfolgen, so dass die abgeschiedenen Teilchen leichter von der Oberfläche des Tellers in den Feststoff räum abrutschen. After the particles have been deposited in step d), it is advantageously possible for the electric field to be switched off and / or discharged on the disk package, so that the deposited particles more easily slip off the surface of the disk into the solids.
Während der Umpolung oder dem Ausschalten des elektrischen Feldes verringert sich der Abscheidungsgrad um einige Prozent. Um daher überflüssiges Umpolen oder Ausschalten vorteilhaft zu vermeiden, kann das Abscheiden, beispielsweise durch eine Sonde an einem Produktablauf der flüssigen Phase bzw. Flüssigphase, überwacht werden. Überschreitet der Anteil an Feststoffen einen vorgegebenen Wert, so ist die Abscheidung auf den Teller ungenügend. Durch die Überwachung der Abscheidung kann das Verfahren an das jeweilige Produkt angepasst werden. Alternativ kann während des Umpolens bzw. Ausschaltens des elektrischen Feldes der Zulauf geschlossen werden. During the polarity reversal or the switching off of the electric field, the degree of separation decreases by a few percent. Therefore, in order to advantageously avoid unnecessary polarity reversal or switch-off, the deposition can be monitored, for example by a probe on a product outlet of the liquid phase or liquid phase. If the proportion of solids exceeds a predetermined value, the deposition on the plate is insufficient. By monitoring the deposition, the process can be adapted to the respective product. Alternatively, the feed can be closed during the polarity reversal or switching off of the electric field.
Erfindungsgemäß weist eine Zentrifuge, insbesondere Separator, eine Zentri- fugentrommel, insbesondere eine kontinuierlich betreibbare Separatortrommel mit vertikaler Drehachse, auf, in der ein Tellerpaket angeordnet ist, wobei die Zentrifugentrommel zumindest einen Produktzulauf zum Zuführen eines zu verarbeitenden Produktes, ein Tellerpaket zur Phasentrennung und wenigstens einen Ablauf zum Ableiten einer flüssigen Phase und einen Ablauf zum Ablei- ten wenigstens einer weiteren Phase, insbesondere einer flüssigen Phase oder einer Feststoffphase, aufweist. Die Zentrifuge weist zudem zumindest ein Mittel auf, zur Erzeugung einer elektrischen Ladung auf den Tellern des Tellerpakets bzw. in Tellerspalten des Tellerpakets. Bei einem Separator mit elektrostatisch aufgeladenen Tellern, erfolgt ein Abscheiden von Teilchen in dem Bereich einer Zentrifuge, an welcher auch üblicherweise die Abscheidung ohne den zusätzlichen Einfluss von Elektrostatik erfolgt. Sofern ein Produkt mit aufgeladenen Teilchen mit der Zentrifuge verarbeitet wird, wird die Abscheidungsrate dieser geladenen Teilchen verbessert, zudem wird ein Kreuzen der bereits abgeschiedenen Teilchen mit dem Produktzulaufstrom verhindert. According to the invention, a centrifuge, in particular a separator, a centrifuge drum, in particular a continuously operable separator drum with a vertical axis of rotation, in which a disc package is arranged, wherein the centrifuge drum at least one product feed for supplying a product to be processed, a disc pack for phase separation and at least an outlet for draining a liquid phase and a drain for discharging at least one further phase, in particular a liquid phase or a solid phase. The centrifuge also has at least one means for generating an electric charge on the plates of the plate package or in plate columns of the plate package. In a separator with electrostatically charged plates, particles are deposited in the region of a centrifuge, at which the deposition usually takes place without the additional influence of electrostatics. When a product containing charged particles is processed by the centrifuge, the deposition rate of these charged particles is improved, and crossing of the already deposited particles with the product feed stream is prevented.
Vorteilhafte Ausgestaltungen der erfindungsgemäßen Zentrifuge sind Gegenstand der Unteransprüche. Advantageous embodiments of the centrifuge according to the invention are the subject of the dependent claims.
Zur Erzeugung einer elektrischen Ladung auf den Tellern eines Tellerpakets kann eine geeignete Gleichspannungsquelle genutzt werden, wobei die Höhe der erzeugten Spannung vorzugsweise verstellbar ist. Dabei liegt an einer Stelle des Separators ein positiver Pol an und an einer anderen Stelle des Separa- tors ein negativer Pol. Einer der Pole steht leitend mit dem Tellerpaket in Verbindung. Dabei ist das Tellerpaket durch eine Beschichtung oder sonstiges nichtleitendes Material von der Außenwandung der Zentrifugentrommel elektrisch isoliert, so dass es nicht durch Kontakt der beiden Bauelemente zu einem Kurzschluss kommen kann. To generate an electrical charge on the plates of a plate package, a suitable DC voltage source can be used, wherein the height of the generated voltage is preferably adjustable. In this case, a positive pole is present at one point of the separator and a negative pole at another point of the separator. One of the poles is conductively connected to the plate package. In this case, the disk pack is electrically insulated from the outer wall of the centrifuge drum by a coating or other non-conductive material, so that it can not come to a short circuit due to contact of the two components.
Ein geeignetes Spannungsniveau für eine solche Gleichspannungsquelle liegt im Bereich zwischen 5000 und 20000 Volt. Um eine einfache Bedienbarkeit zu ermöglichen, ist das Mittel zur Erzeugung einer elektrischen Ladung auf den Tellern des Tellerpakets vorzugsweise außerhalb der Zentrifugentrommel angeordnet. In einer vorteilhaften Ausgestaltung kann ein erster Pol der Gleichspannungsquelle mit positiver oder negativer Ladung an der Außenwandung eines Pumpenelementes der Zentrifuge angeordnet sein, der mit dem Tellerpaket verbunden ist. Dazu muss der Pol lediglich am Pumpenelement angebracht werden, weitere konstruktive Anpassungen der Zentrifugentrommel sind nicht notwen- dig. Dies ist von Vorteil, da somit auch eine bereits existierende Zentrifuge noch nachgerüstet werden kann. A suitable voltage level for such a DC voltage source is in the range between 5000 and 20,000 volts. In order to allow easy operation, the means for generating an electric charge on the plates of the plate package is preferably arranged outside the centrifuge drum. In an advantageous embodiment, a first pole of the DC voltage source can be arranged with positive or negative charge on the outer wall of a pump element of the centrifuge, which is connected to the plate package. For this purpose, the pole only has to be attached to the pump element, further design adjustments of the centrifuge drum are not necessary. This is advantageous, since thus an already existing centrifuge can still be retrofitted.
Nachfolgend wird die Erfindung anhand eines Ausführungsbeispiels anhand einer Zeichnung näher beschrieben. Es zeigt: The invention will be described in more detail with reference to an embodiment with reference to a drawing. It shows:
Fig.1 eine geschnittene Teilansicht einer Separatortrommel in hermetisch geschlossener Bauart. 1 is a partial sectional view of a separator drum in a hermetically sealed design.
Eine drehbare Separatortrommel 1 mit vertikaler Drehachse D ist auf eine Drehspindel 2 gesetzt, welche mit einem Direktantrieb oder durch einen Riemenantrieb, hier nicht dargestellt, angetrieben wird. A rotatable Separatortrommel 1 with vertical axis of rotation D is set to a rotary spindle 2, which is driven by a direct drive or by a belt drive, not shown here.
Die Drehspindel 2 ist entlang eines oberen Umfangsbereichs konisch geformt und mit einem Befestigungsmittel 6 am Trommelunterteil 20 befestigt. The rotary spindle 2 is conically shaped along an upper circumferential region and fastened with a fastening means 6 on the drum base 20.
An einen Produktzulauf 4 schließt sich ein sich im Betrieb mit drehendes Produktzulaufrohr 5 an, welches konzentrisch zur Drehachse D ausgerichtet ist. Aus dem Produktzulaufrohr 5 läuft das Produkt P in einen Verteiler 7 mit Verteilerbohrungen oder -rippen, aus denen das fließfähige Produkt z.B. in radialer Richtung in das Innere der Separatortrommel 1 austreten kann. Denkbar ist es auch (hier nicht dargestellt), das Produkt aus dem Verteiler in wenigstens einen Steigekanal im Tellerpaket zu leiten. A product inlet 4 is adjoined by a product inlet pipe 5 which rotates during operation and which is aligned concentrically with the axis of rotation D. From the product feed tube 5, the product P passes into a manifold 7 having manifold bores or fins from which the flowable product is e.g. can emerge in the radial direction in the interior of the separator drum 1. It is also conceivable (not shown here) to direct the product from the distributor into at least one rising channel in the plate package.
Im Inneren der Separatortrommel 1 fließt das zulaufende Produkt in Tellerspal- te zwischen axial mittel Abstandhaltern voneinander beabstandeten konischen Tellern eines Tellerpakets 1 1 . In the interior of the separator drum 1, the incoming product flows into the plate gap between conical plates of a plate package 1 1 spaced apart from one another by axially intermediate spacers.
In den Tellerspalten erfolgt ein Klären des Produktes (und ggf. auch eine Trennung in zwei oder mehr Flüssigkeitsphasen), indem sich Feststoffteilchen des fließfähigen Produktes an den Tellerunterseiten abscheiden, die von dort in einen Feststoffsammeiraum 8 austreten können. Von dort aus wird die Feststoffphase SP hier diskontinuierlich in radialer Richtung über Feststoffaustrags- öffnungen 1 0 aus der Separatortrommel 1 abgeführt, welche über einen Kol- benschieber 9 geöffnet und geschlossen werden können. Die flüssige Phase LP wird zu einem Pumpenelement 1 2 geleitet und von dort durch einen Produktablauf 1 3 abgeleitet. In the plate columns clarification of the product (and possibly also a separation into two or more liquid phases) takes place by solid particles of the flowable product deposited on the undersides of the plates, which can emerge from there into a Feststoffsammeiraum 8. From there, the solid phase SP is discharged here discontinuously in the radial direction via solids discharge openings 10 from the separator drum 1, which can be opened and closed via a piston slide 9. The liquid phase LP is passed to a pump element 1 2 and discharged from there through a product outlet 1 3.
Eine bessere Abscheidung von Feststoffteilchen in den Tellerspalten eines Tel- lerpakets wird im vorliegenden Fall durch Beaufschlagung des Tellerpakets 1 1 mit einer elektrischen Ladung ermöglicht. Dies führt auch dazu, dass bereits abgeschiedene Teilchen an der Tellerunterseite haften bleiben. A better separation of solid particles in the disk columns of a Teller package is made possible in the present case by applying the plate package 1 1 with an electric charge. This also means that already deposited particles stick to the underside of the plate.
Hierfür ist eine Außenwandung 1 8 der Separatortrommel 1 bzw. eine Außen- wandung 1 9 des Pumpenelements 1 2 über jeweils eine elektrische Leitung 1 5a bzw. 1 5b mit einem positiven und einem negativen Pol einer Gleichspannungsquelle 14 verbunden. For this purpose, an outer wall 1 8 of the separator drum 1 or an outer wall 1 9 of the pump element 1 2 via a respective electrical line 1 5a and 1 5b connected to a positive and a negative pole of a DC voltage source 14.
Ein gut von außen zugängliches Bauteil, hier die Außenwandung 1 9 des Pum- penelements 12, besteht aus einem elektrisch-leitenden Material und ist leitend mit dem Tellerpaket verbunden, so dass dieses je nach Anschluss an die Gleichspannungsquelle positiv oder negativ geladen wird. Ein anderes Bauteil, wie z.B. die eigentliche Separatortrommel 1 wird entgegengesetzt gepolt. Um einen Kurzschluss zu vermeiden, ist das Tellerpaket 1 1 zur Innenwandung der Separatortrommel 1 isoliert, hier durch eine oder mehrere nichtleitende Materialschichten 1 6, 1 7 oberhalb und unterhalb des Tellerpakets 1 1 . Der Verteiler 7 ist zudem durch eine obere Materialschicht 1 7 und eine untere Materialschicht 21 isoliert. A well accessible from the outside component, here the outer wall 1 9 of the pump element 12, consists of an electrically-conductive material and is conductively connected to the plate package, so this is positively or negatively charged depending on the connection to the DC voltage source. Another component, such as the actual separator drum 1 is polarized in the opposite direction. In order to avoid a short circuit, the plate package 1 1 is insulated from the inner wall of the separator drum 1, here by one or more non-conductive material layers 1 6, 1 7 above and below the plate package 1 first The distributor 7 is also insulated by an upper material layer 1 7 and a lower material layer 21.
Zusätzlich dazu kann auch das Trommelunterteil 20 gegen die Drehspindel 2 durch eine elektrisch nichtleitende Materialschicht 22 isoliert sein. In addition, the drum base 20 may also be insulated from the rotary spindle 2 by an electrically non-conductive material layer 22.
Das Produktzulaufrohr 5 und der Verteiler 7 bestehen vorzugsweise aus einem elektrisch nichtleitendem Material oder weisen eine nichtleitende Beschichtung auf, damit die vorzugsweise vor dem Eintritt in die Trommel bereits geladenen Teile sich nicht bereits hier an den Bauelementen absetzen oder entladen. Im Folgenden wird die Funktionsweise des Separators von Fig. 1 anhand eines Verfahrens zur Verarbeitung, insbesondere zur Klärung, eines fließfähigen Produktes näher erläutert. Ergänzend erfolgt eine Vorbehandlung nach Art des Schrittes a) des Anspruchs 1 . Nach einer Variante dieser Vorbehandlung wird das Produkt zunächst vor dem Eintritt in die sich drehende Separatortrommel an einer negativ oder positiv geladenen Elektrode einer Gleichspannungsquelle vorbeigeführt, so dass sich die Feststoffteilchen im Produkt elektrisch aufladen. Diese Elektrode kann auch alternativ im Produktzulauf 4 oder im Zulaufrohr 5 angeordnet sein. Das Laden der Feststoffteilchen kann aber auch an anderer Stelle vor dem Eintritt des Produktstromes in den Tellerspalt des Tellerpakets 1 1 erfolgen. Ein geeignetes Spannungsniveau für eine solche Gleichspannungsquelle liegt im Bereich zwischen 5000 und 20000 Volt. The product inlet pipe 5 and the manifold 7 are preferably made of an electrically non-conductive material or have a non-conductive coating, so that preferably already charged before entering the drum parts not settle or unload here already on the components. In the following, the mode of operation of the separator of FIG. 1 will be explained in more detail by means of a method for processing, in particular for clarification, of a flowable product. In addition, a pretreatment in the manner of step a) of claim 1. According to a variant of this pre-treatment, the product is first passed before entering the rotating separator drum to a negative or positive charged electrode of a DC voltage source, so that the solid particles in the product charge electrically. This electrode can also be arranged alternatively in the product feed 4 or in the feed pipe 5. The loading of the solid particles can also be done elsewhere before the entry of the product flow in the plate gap of the plate package 1 1. A suitable voltage level for such a DC voltage source is in the range between 5000 and 20,000 volts.
Sofern das Aufladen der Feststoffteilchen vor dem Eintritt des fließfähigen Produktstroms in den Separator erfolgt, ist es von Vorteil, wenn das Produktzuleitungsrohr 5 und der Verteiler 7 aus nichtleitendem Material bestehen oder mit nichtleitendem Material beschichtet sind, damit das Abscheiden vorzugsweise nur im Tellerpaket erfolgt. If the charging of the solid particles takes place prior to the entry of the flowable product stream into the separator, it is advantageous if the product supply pipe 5 and the distributor 7 consist of non-conductive material or are coated with non-conductive material, so that the deposition preferably takes place only in the disk package.
Nach dem Einlauf des Produktes in die Trommel 1 tritt es in die Tellerspalte des Tellerpakts 1 1 ein. Dabei ist die Ladung der Teilchen des Produkts entgegengesetzt zur Ladung der Teller, so dass der Teller eine elektrostatische An- Ziehung auf die geladenen Teilchen ausübt, die sich vermehrt an den Tellern sammeln. Die Tellerspalte setzen sich daher mit der Zeit immer weiter zu. After the product has entered the drum 1, it enters the plate column of the plate pack 1 1. In this case, the charge of the particles of the product is opposite to the charge of the plates, so that the plate exerts an electrostatic attraction on the charged particles, which collect increasingly on the plates. The plate column therefore continue to grow over time.
Durch ein Umpolen oder Ausschalten der Gleichspannungsquelle 14 erfolgt sodann ein Abstoßen der angesammelten Teilchen, insbesondere der Fest- Stoffteilchen, von der Telleroberfläche und ein Transport der Feststoffteilchen in den Feststoffsammeiraum 8 (vorzugsweise bei unterbrochenem Zulauf). By reversing or switching off the DC voltage source 14, there is then a repulsion of the accumulated particles, in particular of the solid particles, from the plate surface and a transport of the solid particles into the Feststoffsammeiraum 8 (preferably with interrupted feed).
Wie bereits erläutert, setzt sich das Tellerpaket mit der Zeit zu. Daher ist es von Vorteil, wenn dies (z.B. anhand der Zulaufmenge oder der Ablaufmenge) im Betrieb geeignet überwacht wird und wenn in Abhängigkeit von der Überwachung - oder periodisch in vorgegebenen Zeitabständen - eine Umpolung des Tellerpakets und ggf. eine Entleerung der Trommel erfolgt, um die angesetzten Teilchen auszuspülen. Hierzu ist die Gleichspannungsquelle vorzugsweise an das Steuer- und Regelsystem der Zentrifuge angeschlossen (hier nicht dargestellt). As already explained, the plate package increases with time. It is therefore advantageous if this is suitably monitored during operation (for example based on the inflow quantity or the outflow quantity) and if, depending on the monitoring or periodically at predetermined time intervals, the plate package is reversed and, if appropriate, the drum is emptied rinse out the attached particles. For this purpose, the DC voltage source is preferably on connected the control system of the centrifuge (not shown here).
In Fig.1 ist ein Separator abgebildet, welcher eine Fest-Flüssig-Trennung er- möglicht. Allerdings kann das Verfahren analog auch auf Drei-Phasen- Separatoren angewandt werden. Alternativ zur Bauform eines Separators, bei dem die Separatortrommel 1 auf eine Drehspindel 2 aufgesetzt ist, kann die Abscheidung von Feststoffen auf einem aufgeladenen Tellerpaket bei anderen Bauformen z.B. mit hängenden Trommeln eingesetzt werden. FIG. 1 shows a separator which allows a solid-liquid separation. However, the method can also be applied analogously to three-phase separators. As an alternative to the design of a separator in which the separator drum 1 is mounted on a rotary spindle 2, the deposition of solids on a charged plate package in other designs, e.g. be used with hanging drums.
Das erfindungsgemäße Verfahren und die Zentrifuge eignen sich für verschiedenste Produkte, insbesondere jedoch zur Reinigung eines verunreinigten Öls. Anzumerken ist noch, dass die Ausgestaltung als hermetisch geschlossene Maschine mit drehendem Zulaufrohr und einem anleitenden Pumpenelement, bei welcher das Produkt durch die Maschine gepumpt wird, zwar bevorzugt wird, nicht aber zwingend ist. The inventive method and the centrifuge are suitable for a wide variety of products, but in particular for the purification of a contaminated oil. It should also be noted that although the embodiment is preferred as a hermetically sealed machine with rotating inlet pipe and an instructive pump element, in which the product is pumped through the machine, it is not mandatory.
Bezugszeichenliste LIST OF REFERENCE NUMBERS
1 Separatortrommel 1 separator drum
2 Drehspindel 2 rotary spindle
4 Produktzulauf 4 product feed
5 Produktzulaufrohr 5 product inlet pipe
6 Befestigungsmittel 6 fasteners
7 Verteiler 7 distributors
8 Feststoff sam mel rau m 8 solid sam mel m
9 Kolbenschieber 9 piston valve
10 Feststoff austragsöffnung 10 solids discharge opening
1 1 Tellerpaket 1 1 plate pack
12 Pumpenelement 12 pump element
13 Produktablauf 13 product flow
14 Gleichspannungsquelle 14 DC voltage source
15a, b Stromleitungen 15a, b power lines
1 6 nichtleitende Materialschichten 1 6 non-conductive material layers
17 nichtleitende Materialschichten17 non-conductive material layers
18 Außenwand Separatortrommel18 outer wall separator drum
19 Außenwand Pumpenelement19 outer wall pump element
20 Trommelunterteil 20 drum base
21 nichtleitende Materialschichten 21 non-conductive material layers
22 nichtleitende Materialschichten22 non-conductive material layers
D Drehachse D rotation axis
SP Feststoffphase SP solid phase
LP Flüssigkeitsphase LP liquid phase
P Produkt P product
Claims
Applications Claiming Priority (2)
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DE102017125057.3A DE102017125057A1 (en) | 2017-10-26 | 2017-10-26 | Process for processing a flowable product and centrifuge |
PCT/EP2018/078970 WO2019081469A1 (en) | 2017-10-26 | 2018-10-23 | Method for processing a flowable product and centrifuge |
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EP3700678A1 true EP3700678A1 (en) | 2020-09-02 |
EP3700678B1 EP3700678B1 (en) | 2023-08-30 |
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EP18795413.6A Active EP3700678B1 (en) | 2017-10-26 | 2018-10-23 | Method for processing a flowable product and centrifuge |
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US (1) | US11660612B2 (en) |
EP (1) | EP3700678B1 (en) |
CN (1) | CN111212690A (en) |
AR (1) | AR113788A1 (en) |
DE (1) | DE102017125057A1 (en) |
WO (1) | WO2019081469A1 (en) |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1558382A (en) * | 1923-07-13 | 1925-10-20 | Marx Alfred | Electrocentrifugal separator |
US3126338A (en) * | 1959-11-30 | 1964-03-24 | Hermetically sealable mounting means | |
NL128415C (en) * | 1963-01-26 | |||
SU551036A1 (en) | 1974-06-10 | 1977-03-25 | Ленинградский Ордена Трудового Красного Знамени Инженерно-Строительный Институт | Electric Centrifugal Cleaner |
DE2916856A1 (en) * | 1979-04-26 | 1980-11-06 | Hoechst Ag | SEPARATOR |
JPH0278454A (en) * | 1988-09-14 | 1990-03-19 | Mitsubishi Agricult Mach Co Ltd | Centrifugal electrostatic oil cleaner |
JPH082427B2 (en) * | 1989-10-25 | 1996-01-17 | 三菱農機株式会社 | Detection structure in centrifugal electrostatic oil purifier |
RU2091168C1 (en) * | 1995-12-04 | 1997-09-27 | Акционерное общество научно-производственное предприятие "Конверсия" | Apparatus for purifying dielectric liquids |
SE527934C2 (en) * | 2004-06-03 | 2006-07-11 | Alfa Laval Corp Ab | An apparatus and method for purifying a gas |
SE528750C2 (en) * | 2005-06-27 | 2007-02-06 | 3Nine Ab | Method and apparatus for separating particles from a gas stream |
DE102006022156A1 (en) * | 2006-05-12 | 2007-11-29 | Westfalia Separator Ag | Method and device for the treatment of liquids |
US20160375447A1 (en) * | 2015-06-24 | 2016-12-29 | Hirata Corporation | Electric dust collector of cyclone separator |
-
2017
- 2017-10-26 DE DE102017125057.3A patent/DE102017125057A1/en not_active Withdrawn
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2018
- 2018-10-23 US US16/759,069 patent/US11660612B2/en active Active
- 2018-10-23 CN CN201880066845.7A patent/CN111212690A/en active Pending
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- 2018-10-23 AR ARP180103086A patent/AR113788A1/en active IP Right Grant
- 2018-10-23 WO PCT/EP2018/078970 patent/WO2019081469A1/en unknown
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WO2019081469A1 (en) | 2019-05-02 |
US11660612B2 (en) | 2023-05-30 |
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DE102017125057A1 (en) | 2019-05-02 |
CN111212690A (en) | 2020-05-29 |
EP3700678B1 (en) | 2023-08-30 |
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