EP1616627B1 - High gradient magnetic separator - Google Patents
High gradient magnetic separator Download PDFInfo
- Publication number
- EP1616627B1 EP1616627B1 EP05008969.7A EP05008969A EP1616627B1 EP 1616627 B1 EP1616627 B1 EP 1616627B1 EP 05008969 A EP05008969 A EP 05008969A EP 1616627 B1 EP1616627 B1 EP 1616627B1
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- European Patent Office
- Prior art keywords
- gradient magnetic
- magnetic separator
- matrix
- separation
- separator according
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- 239000006148 magnetic separator Substances 0.000 title claims description 29
- 239000011159 matrix material Substances 0.000 claims description 50
- 238000000926 separation method Methods 0.000 claims description 50
- 239000002245 particle Substances 0.000 claims description 19
- 239000012530 fluid Substances 0.000 claims description 17
- 239000000725 suspension Substances 0.000 claims description 15
- 238000011010 flushing procedure Methods 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 5
- 239000011888 foil Substances 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims 1
- 238000007789 sealing Methods 0.000 claims 1
- 230000005291 magnetic effect Effects 0.000 description 20
- 238000004140 cleaning Methods 0.000 description 18
- 239000006249 magnetic particle Substances 0.000 description 9
- 230000008021 deposition Effects 0.000 description 6
- 125000006850 spacer group Chemical group 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000007885 magnetic separation Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000000087 stabilizing effect Effects 0.000 description 4
- 238000002156 mixing Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000005294 ferromagnetic effect Effects 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 210000002268 wool Anatomy 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 229910052622 kaolinite Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- 230000005415 magnetization Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 230000005298 paramagnetic effect Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000008237 rinsing water Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
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- 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
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/033—Component parts; Auxiliary operations characterised by the magnetic circuit
- B03C1/0332—Component parts; Auxiliary operations characterised by the magnetic circuit using permanent magnets
-
- 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
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/029—High gradient magnetic separators with circulating matrix or matrix elements
- B03C1/03—High gradient magnetic separators with circulating matrix or matrix elements rotating, e.g. of the carousel type
-
- 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
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/032—Matrix cleaning systems
Definitions
- the invention relates to a high-gradient magnetic separator according to the preamble of the first claim.
- the separation of ferro-, ferri- or paramagnetic particles from liquid or gaseous fluids by means of magnetic separators is a basic principle of process technology used in numerous variants.
- a particular advantage of the principle of magnetic separation is the ability to selectively separate magnetic particles from a mixture with other non-magnetic particles.
- the choice of the magnetic separator depends on the size and the magnetic properties of the particles.
- Coarse strong magnetic particles e.g. Magnetic ores with particle sizes> 75 ⁇ m can then be separated with simple drum or belt separators. Fine, strongly magnetic particles can also be detected from aqueous suspensions up to a size of about 10-20 ⁇ m by means of special drum separators. For even finer particles in the micrometer range (about 0.1 to 20 microns), however, so far only so-called high-gradient magnetic separation is used.
- the functional principle of high-gradient magnetic separators is based on the generation and bundling of strong field strength gradients by introducing a ferromagnetic matrix into an external magnetic field.
- the magnetizable elements of the matrix usually consist of disordered steel wool or ordered wire nets or profiled metal plates. They are magnetized by the external field and in turn form magnetic poles that reinforce or weaken the outer field in places.
- the resulting, high field strength gradients result in a strong magnetic force on para- or ferromagnetic particles in the direction of higher field strength.
- the Particles attach themselves to the induced magnetic poles of the matrix and are thus separated from the fluid.
- the loading of the separator with separated magnetizable particles are so high that the capacity of the magnetic separator is exhausted and a matrix cleaning is required.
- the matrix cleaning is carried out after switching off the magnetic field with a strong water jet or a backwash with high filter speeds. Due to the shape and structure of the matrix, which consists for example of steel wool or layered wire mesh and thus has numerous spaces, so-called dead volumes occur in the area of the matrix, ie areas which are not or only very slowly flowed through.
- the desire to keep the volume of the resulting rinse concentrate as low as possible and the maximum flow rate of the pump, the amount of flushing fluid used and the achievable flow rate during the flushing process. As a result, only incomplete cleaning is achieved. In particular, particles with a high remanent magnetization are difficult to remove again. The consequence is a further strong adhesion of these particles to the matrix wires, which significantly affects the cleaning efficiency.
- complete matrix cleaning is not absolutely necessary, but desirable and economically desirable to utilize the separator capacity.
- the matrix cleaning is carried out by rinsing water at high flow rates in countercurrent.
- the invention consists of a high-gradient magnetic separator for the selective deposition of magnetisable particles from a suspension, comprising a matrix which can be positioned in a magnet system as a separation zone.
- the matrix is subdivided into plate-shaped partial volumes by plate-shaped magnetizable separation surfaces through which the suspension can flow. Furthermore, it has areas that serve as an inlet or as a drain of the suspension, wherein at least one, more preferably two separation surfaces are preferably arranged between an inlet and a drain.
- the matrix preferably extends over a closed volume, the inlets and outlets being formed by concrete lines into this volume.
- the separation surfaces are preferably formed by wire mesh or perforated metal foils or sheets, and may be provided with trapping structures for trapping forces from fluid flow or for clamping and securing.
- the selective separation of magnetic particles from a suspension it is passed as a fluid flow via the inlet into the matrix and through this in at least one, preferably two separation surfaces. After passing through the separation surfaces of the fluid flow leaves the matrix through a drain, wherein the magnetizable particles are magnetically retained on the separation surfaces.
- An essential design feature of the invention and with a particularly advantageous effect in matrix cleaning is the subdivision of the separation surfaces into at least two groups.
- the separation surfaces of each group are mechanically, for example via a housing, a carrier or a shaft rigidly coupled together and stored in the high gradient magnetic separator either fixed or movably mounted.
- the separation surfaces are preferably subdivided into two groups, wherein the group membership of the separation surfaces, which are preferably arranged parallel to one another in the matrix, alternates.
- a group is firmly inserted in the housing and the second group is jointly provided on a movably mounted carrier wherein an alternating arrangement of the separation surfaces of the different groups in the matrix.
- the movably mounted carrier is preferably motor-driven or actuator-driven, with the executable movement being cyclic, ie rotational and / or translationally oscillating in one or more directions.
- the carrier comprises a rotatably and / or laterally movably mounted shaft around which the matrix and the separation surfaces extend rotationally symmetrically.
- the frequency of the rotary or oscillating relative movement is usually between 5 and 1000 Hz, depending on the structural design.
- the abovementioned mutually movable separation surface groups are not absolutely necessary.
- a moderate relative movement of adjacent separation surfaces to one another promotes the thorough mixing of the suspension and thus the more uniform detection of the entire suspension volume during the deposition and a more uniform separation of magnetizable particles on the available separation surfaces. From a certain strength, the relative movements prevent a stable settling of the particles on the separation surfaces, thus counterproductive and should be avoided during the deposition.
- the matrix cleaning is preferably carried out according to the countercurrent principle with a flushing fluid, wherein the relative movement of at least two of the aforementioned separation surface fractions to each other in the flushing fluid causes inertial forces, centrifugal forces, turbulence and shear forces, which detachment of magnetizable particles from the separation surfaces even in the presence of magnetic remanence or in the Influence of a magnetic field significantly improved or even only possible.
- the high-gradient magnetic separator 1 is in the immediate range of action of a magnet system 2, which serves as a field source.
- the magnetic field source is preferably electromagnets ( Fig. 1 ), superconducting magnet systems or even permanent magnet systems ( FIG. 2 ), wherein the high-gradient magnetic separator 1 is introduced into the magnet coil opening or between the pole shoes 3.
- the actual high-gradient magnetic separator comprises a plurality of subunits, namely a substantially cylindrical housing 5, which is axially closed with a lid 6 and a bottom 7.
- a shaft 8 is mounted concentrically in the housing, in the embodiment in corresponding bearings 9 in the lid and / or bottom, sealingly rotatable and connected via a coupling 10 with a drive 11.
- Shaft, housing, cover and base plate are made of a non-magnetic material.
- the core unit of the high-gradient magnetic separator is the matrix, which extends over the enclosed space enclosed by the housing 5, cover 6 and bottom 7 and in which the deposition of magnetizable particles takes place.
- the suspension (fluid) with the magnetic particles to be separated enters the high-gradient magnetic separator via the inlet 4 and is distributed over the separator cross-section. The actual separation takes place in the region of the matrix on Separationsringusionn 13 and 14.
- the purified fluid stream leaves the high-gradient magnetic separator on the flow 12.
- inlet and outlet consist of several openings in the lid 6 and bottom 7 and have for better flow distribution in each case one conical shape.
- the matrix is constructed according to the rotor-stator principle (cf. Fig. 3 and 4 ) and alternately comprises the aforementioned concentric arranged around the shaft and inserted in the housing 5 fixed and placed on the shaft 8 rotating separation ring discs 13 and 14, which divides the interior volume into rotationally symmetrical and axially successively arranged partial volumes.
- the separation ring disks 13 and 14, in detail in FIG Fig. 5 each comprise a separation surface 15 of magnetizable material, preferably a wire mesh or a perforated metal foil or sheet, which can be flowed through by the suspension.
- the separation surface 15 is bounded by an outer and an inner stabilizing ring 16 and 17, respectively.
- the rotating Separationsringsayn 14 are mounted on the inner stabilizing rings 17 alternately with non-magnetic inner spacers 18 on the shaft 8 and clamped axially with a clamping sleeve 19.
- the fixed Separationsringin 13 are alternately inserted via the outer stabilizing rings 16 with non-magnetic outer spacer sleeves 20 in the housing 5 and clamped by a sleeve 21.
- the respective non-clamped inner and outer stabilizing rings 17 and 16 respectively form inner and outer spacer sleeves 18 and 20 an annular gap (see. Fig. 3 and 4 ).
- Fig. 3 shows an embodiment with fluidly connected in series subvolumes in the matrix.
- Fig. 4 represents an alternative concept with fluidically connected Operavolumna in the matrix.
- the feeding of the suspension with the magnetic particles to be separated takes place via a designed as a hollow shaft shaft 8 and a plurality of these branching radial inlet holes 22 as suspension outlets in each second of the partial volumes of the matrix.
- the flow of the purified fluid flow takes place from the partial volumes without direct inlet bore via drain holes 23, which open into a collecting channel 24, formed by the interior of a double-walled housing 25.
- Inlet and drain bores 22 and 23 are each arranged offset, so that when flowing through the matrix at least one separation ring disk is flowed through.
- a matrix cleaning is done from time to time, preferably in countercurrent process.
- the criterion for the cleaning intervals is the pressure drop in the separator, which correlates with the loading of the sedimentation ring disks and indicates the need for matrix cleaning when exceeding a certain value.
- a flushing fluid is passed from the flow through the partial volumes to the inlet, the shaft 8 are rotated with the rotating separation ring disks 13 at high speed (about 100 to 500 rev / min). The resulting shearing in the fluid flow creates turbulences which entrain the magnetic particles deposited on the separation ring disks. The separated particles will then be removed from the matrix by the superimposed purge fluid stream.
- the efficiency of the cleaning can be further improved by the fact that the high-gradient magnetic separator 1 is deprived of the influence of a magnetic field.
- the magnetic field can now be switched off or the high-gradient magnetic separator can be removed from the magnetic field.
- an oscillation movement can alternatively be transmitted to the shaft 8.
- An additional force can be built up if the shaft oscillates axially by corresponding drive and bearing in addition to a rotational movement.
- the hydrodynamics in the filter can be influenced and thus a flow channel formation is suppressed.
- the structure of the matrix proposed in the exemplary embodiments enables a modular and flexible construction of the high-gradient magnetic separator.
- the number and spacing of the sub-volumes and separation ring disks can be varied in a simple manner and, according to a modular principle, also for subregions of the matrix.
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- Centrifugal Separators (AREA)
Description
Die Erfindung betrifft einen Hochgradienten-Magnetabscheider gemäß dem Oberbegriff des ersten Patentanspruchs.The invention relates to a high-gradient magnetic separator according to the preamble of the first claim.
Die Abtrennung ferro-, ferri- oder paramagnetischer Partikel aus flüssigen oder gasförmigen Fluiden mittels Magnetscheider ist ein in zahlreichen Varianten genutztes Grundprinzip der Verfahrenstechnik. Ein besonderer Vorteil des Prinzips der Magnetscheidung liegt in der Möglichkeit, magnetische Partikel aus einer Mischung mit anderen nicht magnetischen Partikeln selektiv abzutrennen. Die Wahl des Magnetscheiders richtet sich dabei nach der Größe und den magnetischen Eigenschaften der Partikel.The separation of ferro-, ferri- or paramagnetic particles from liquid or gaseous fluids by means of magnetic separators is a basic principle of process technology used in numerous variants. A particular advantage of the principle of magnetic separation is the ability to selectively separate magnetic particles from a mixture with other non-magnetic particles. The choice of the magnetic separator depends on the size and the magnetic properties of the particles.
Grobe stark magnetische Partikel, wie z.B. Magnetiterze mit Partikelgrößen > 75µm lassen sich danach bereits mit einfachen Trommel- oder Bandscheidern abtrennen. Feinere stark magnetische Partikel lassen sich aus wässrigen Suspensionen bis zu einer Größe von ca. 10-20 µm ebenfalls noch mittels spezieller Trommelscheider erfassen. Für noch feinere Partikel im Mikrometerbereich (ca. 0,1 bis 20 µm) kommt dagegen bisher nur sogenannte Hochgradienten-Magnetseparation zum Einsatz.Coarse strong magnetic particles, e.g. Magnetic ores with particle sizes> 75μm can then be separated with simple drum or belt separators. Fine, strongly magnetic particles can also be detected from aqueous suspensions up to a size of about 10-20 μm by means of special drum separators. For even finer particles in the micrometer range (about 0.1 to 20 microns), however, so far only so-called high-gradient magnetic separation is used.
Das Funktionsprinzip von Hochgradienten-Magnetseparatoren beruht auf der Generierung und Bündelung starker Feldstärkegradienten durch das Einbringen einer ferromagnetischen Matrix in ein äußeres Magnetfeld. Die magnetisierbaren Elemente der Matrix bestehen meist aus ungeordneter Stahlwolle bzw. geordneten Drahtnetzen oder profilierten Metallplatten. Sie werden durch das äußere Feld aufmagnetisiert und bilden ihrerseits Magnetpole aus, die das äußere Feld stellenweise verstärken oder auch abschwächen. Durch die entstehenden, hohen Feldstärkegradienten resultiert eine starke Magnetkraft auf para- bzw. ferromagnetische Partikel in Richtung höherer Feldstärke. Die Partikel lagern sich an den induzierten Magnetpolen der Matrix an und sind damit aus dem Fluid abgeschieden.The functional principle of high-gradient magnetic separators is based on the generation and bundling of strong field strength gradients by introducing a ferromagnetic matrix into an external magnetic field. The magnetizable elements of the matrix usually consist of disordered steel wool or ordered wire nets or profiled metal plates. They are magnetized by the external field and in turn form magnetic poles that reinforce or weaken the outer field in places. The resulting, high field strength gradients result in a strong magnetic force on para- or ferromagnetic particles in the direction of higher field strength. The Particles attach themselves to the induced magnetic poles of the matrix and are thus separated from the fluid.
Durch die Möglichkeit der Generierung sehr hoher Feldgradienten und somit entsprechend hoher Magnetkräfte in Verbindung mit einer feinmaschigen Matrix ist das Verfahren der Hochgradienten-Magnetseparation sehr effektiv, wenn es darum geht, geringe Mengen magnetischer Verunreinigungen aus einer Suspension zu entfernen. Typische Einsatzbeispiele finden sich in der Kaolinitaufbereitung oder in der Entfernung von Korrosionsprodukten aus Kondensatkreisläufen.Due to the possibility of generating very high field gradients and thus correspondingly high magnetic forces in connection with a fine-meshed matrix, the process of high-gradient magnetic separation is very effective when it comes to removing small amounts of magnetic impurities from a suspension. Typical applications are found in kaolinite processing or in the removal of corrosion products from condensate circuits.
Nach einer bestimmten Betriebszeit sind jedoch die Beladung des Separators mit abgeschiedenen magnetisierbaren Partikeln so hoch, dass die Aufnahmekapazität des Magnetabscheiders erschöpft ist und eine Matrixabreinigung erforderlich ist. Üblicherweise erfolgt die Matrixabreinigung nach Abschalten des Magnetfelds mit einem starken Wasserstrahl beziehungsweise einer Rückspülung mit hohen Filtergeschwindigkeiten. Bedingt durch Form und Aufbau der Matrix, die beispielsweise aus Stahlwolle oder geschichteten Drahtgeweben besteht und somit zahlreiche Zwischenräume aufweist, kommt es im bereich der Matrix lokal zu sogenannten Totvolumina, d.h. zu Bereichen, die nicht oder nur sehr langsam durchströmt werden. Zudem begrenzen der Wunsch, das Volumen des anfallenden Spülkonzentrats möglichst gering zu halten sowie die maximale Förderleistung der Pumpen die Menge des eingesetzten Spülfluids und die erreichbare Fließgeschwindigkeit während des Spülvorgangs. Als Folge wird nur eine unvollständige Abreinigung erzielt. Insbesondere Partikel mit einer hohen Remanenzmagnetisierung lassen sich nur schwer wieder entfernen. Die Konsequenz ist eine weiterhin starke Haftung dieser Partikel an den Matrixdrähten, was die Abreinigungseffizienz signifikant beeinträchtigt.After a certain period of operation, however, the loading of the separator with separated magnetizable particles are so high that the capacity of the magnetic separator is exhausted and a matrix cleaning is required. Usually, the matrix cleaning is carried out after switching off the magnetic field with a strong water jet or a backwash with high filter speeds. Due to the shape and structure of the matrix, which consists for example of steel wool or layered wire mesh and thus has numerous spaces, so-called dead volumes occur in the area of the matrix, ie areas which are not or only very slowly flowed through. In addition, the desire to keep the volume of the resulting rinse concentrate as low as possible and the maximum flow rate of the pump, the amount of flushing fluid used and the achievable flow rate during the flushing process. As a result, only incomplete cleaning is achieved. In particular, particles with a high remanent magnetization are difficult to remove again. The consequence is a further strong adhesion of these particles to the matrix wires, which significantly affects the cleaning efficiency.
Während zur Thematik der Partikelabscheidung eine Vielzahl von Patenten und Veröffentlichungen vorhanden ist, liegen auf dem Gebiet der Filterrückspülung und Matrixabreinigung nur sehr wenige Untersuchungen vor. Eine wirkungsvolle und vollständige Matrixabscheidung ist aber wesentlich für viele Anwendungen, allein auch um technischen, ökonomischen sowie ökologischen Rahmenbedingungen gerecht zu werden. Insbesondere dann, wenn die magnetische Abtrennung von magnetisierbaren Partikeln als wichtiger Teilschritt in einen kontinuierlichen Gesamtprozess eingebunden ist, verlangt ein optimaler Filterbetrieb eine Minimierung der Dauer der Matrixabreinigung sowie der hierfür erforderlichen Spülfluidmenge.While a large number of patents and publications are available on the subject of particle separation, there are only a few investigations in the field of filter backwashing and matrix cleaning. An effective and complete matrix deposition is essential for many applications, but also to meet technical, economic and environmental conditions. In particular, when the magnetic separation of magnetizable particles is involved as an important part of a continuous process, optimal filter operation requires a minimization of the duration of the matrix cleaning and the amount of flushing fluid required for this purpose.
Bei bestimmten Anwendungen, beispielsweise im Abwasserbereich, ist eine vollständige Matrixabreinigung nicht unbedingt notwendig, aber wünschenswert und ökonomisch geboten, um die Separatorkapazität auszuschöpfen. Die Matrixabreinigung erfolgt dabei durch Spülwasser mit hohen Fließgeschwindigkeiten im Gegenstrom.In certain applications, for example in the wastewater sector, complete matrix cleaning is not absolutely necessary, but desirable and economically desirable to utilize the separator capacity. The matrix cleaning is carried out by rinsing water at high flow rates in countercurrent.
In der
Ausgehend davon ist es Aufgabe der Erfindung, einen Hochgradienten-Magnetseparator vorzuschlagen, welcher eine mechanisch einfache, robuste, flexible und kostengünstige Vorrichtung zur effizienten Matrixabreinigung umfasst.Proceeding from this, it is an object of the invention to propose a high-gradient magnetic separator, which comprises a mechanically simple, robust, flexible and cost-effective device for efficient matrix cleaning.
Die Aufgabe wird durch die kennzeichnenden Merkmale in Anspruch 1 gelöst; die hierauf bezogenen Unteransprüche beinhalten vorteilhafte Ausführungsformen dieser Lösung.The object is solved by the characterizing features in
Die Erfindung besteht aus einem Hochgradienten-Magnetabscheider zum selektiven Abscheiden magnetisierbarer Partikel aus einer Suspension, umfassend eine in einem Magnetsystem positionierbare Matrix als Separierungszone. Die Matrix wird durch plattenförmige magnetisierbare und von der Suspension durchströmbare Separationsflächen in aneinander gereihte Teilvolumina unterteilt. Ferner weist sie Bereiche auf, die als Zulauf oder als Ablauf der Suspension dienen, wobei vorzugsweise zwischen einem Zulauf und einem Ablauf mindestens eine, weiter bevorzugt zwei Separationsflächen angeordnet sind. Vorzugsweise erstreckt sich die Matrix über ein abgeschlossenes Volumen, wobei die Zuläufe und Abläufe durch konkrete Leitungen in dieses Volumen gebildet werden. Die Separationsflächen werden bevorzugt durch Drahtgewebe oder perforierte Metallfolien oder - bleche gebildet und können zum Auffangen der Kräfte aus einer Fluidströmung oder zum Einspannen und Befestigen mit Verstärkungsstrukturen versehen sein.The invention consists of a high-gradient magnetic separator for the selective deposition of magnetisable particles from a suspension, comprising a matrix which can be positioned in a magnet system as a separation zone. The matrix is subdivided into plate-shaped partial volumes by plate-shaped magnetizable separation surfaces through which the suspension can flow. Furthermore, it has areas that serve as an inlet or as a drain of the suspension, wherein at least one, more preferably two separation surfaces are preferably arranged between an inlet and a drain. The matrix preferably extends over a closed volume, the inlets and outlets being formed by concrete lines into this volume. The separation surfaces are preferably formed by wire mesh or perforated metal foils or sheets, and may be provided with trapping structures for trapping forces from fluid flow or for clamping and securing.
Zum selektiven Abscheiden magnetischer Partikel aus einer Suspension wird diese als Fluidstrom über den Zulauf in die Matrix und in dieser durch mindestens eine, vorzugsweise zwei Separationsflächen geleitet. Nach Durchlaufen der Separationsflächen verlässt der Fluidstrom die Matrix durch einen Ablauf, wobei die magnetisierbaren Partikel magnetisch auf den Separationsflächen zurückgehalten werden.For the selective separation of magnetic particles from a suspension, it is passed as a fluid flow via the inlet into the matrix and through this in at least one, preferably two separation surfaces. After passing through the separation surfaces of the fluid flow leaves the matrix through a drain, wherein the magnetizable particles are magnetically retained on the separation surfaces.
Wesentliches Gestaltungsmerkmal der Erfindung und mit besonders vorteilhafter Wirkung bei einer Matrixabreinigung ist die Unterteilung der Separationsflächen in mindestens zwei Gruppen. Die Separationsflächen jeder Gruppe sind mechanisch beispielsweise über ein Gehäuse, einen Träger oder eine Welle starr miteinander gekoppelt und im Hochgradienten-Magnetseparator entweder fest eingesetzt oder beweglich gelagert. Bevorzugt sind die Separationsflächen in zwei Gruppen unterteilt, wobei sich die Gruppenzugehörigkeit der vorzugsweise parallel zueinander in der Matrix angeordneten Separationsflächen abwechselt. Dabei ist eine Gruppe fest im Gehäuse eingesetzt ist und die zweite Gruppe gemeinsam auf einem beweglich gelagerten Träger wobei eine abwechselnde Anordnung der Separationsflächen aus den verschiedenen Gruppen in der Matrix vorgesehen ist. Der beweglich gelagerte Träger ist vorzugsweise motorisch oder aktorisch angetrieben, wobei die ausführbare Bewegung zyklisch ist, d.h. rotatorisch und / oder in eine oder mehrere Richtungen translatorisch oszillierend. In einer bevorzugten Ausführungsform umfasst der Träger eine drehbar und / oder lateral bewegbar gelagerte Welle, um die sich die Matrix und die Separationsflächen rotationssymmetrisch erstrecken. Die Frequenz der Dreh- bzw. oszillierenden Relativbewegung liegt je nach konstruktiver Gestaltung üblicherweise zwischen 5 und 1000 Hz.An essential design feature of the invention and with a particularly advantageous effect in matrix cleaning is the subdivision of the separation surfaces into at least two groups. The separation surfaces of each group are mechanically, for example via a housing, a carrier or a shaft rigidly coupled together and stored in the high gradient magnetic separator either fixed or movably mounted. The separation surfaces are preferably subdivided into two groups, wherein the group membership of the separation surfaces, which are preferably arranged parallel to one another in the matrix, alternates. In this case, a group is firmly inserted in the housing and the second group is jointly provided on a movably mounted carrier wherein an alternating arrangement of the separation surfaces of the different groups in the matrix. The movably mounted carrier is preferably motor-driven or actuator-driven, with the executable movement being cyclic, ie rotational and / or translationally oscillating in one or more directions. In a preferred embodiment, the carrier comprises a rotatably and / or laterally movably mounted shaft around which the matrix and the separation surfaces extend rotationally symmetrically. The frequency of the rotary or oscillating relative movement is usually between 5 and 1000 Hz, depending on the structural design.
Für das selektive Abscheiden von magnetischen Partikeln aus einer Suspension sind die vorgenannten zueinander bewegbaren Separationsflächengruppen nicht unbedingt erforderlich. Eine moderate Relativbewegung benachbarter Separationsflächen zueinander fördert allerdings die Durchmischung der Suspension und damit die gleichmäßigere Erfassung des gesamten Suspensionsvolumens bei der Abscheidung sowie eine gleichmäßigere Abscheidung von magnetisierbaren Partikeln auf den zur Verfügung stehenden Separationsflächen. Ab einer bestimmten Stärke verhindern die Relativbewegungen ein stabiles Absetzen der Partikel auf den Separationsflächen, wirken somit kontraproduktiv und sind während der Abscheidung zu vermeiden.For the selective deposition of magnetic particles from a suspension, the abovementioned mutually movable separation surface groups are not absolutely necessary. However, a moderate relative movement of adjacent separation surfaces to one another promotes the thorough mixing of the suspension and thus the more uniform detection of the entire suspension volume during the deposition and a more uniform separation of magnetizable particles on the available separation surfaces. From a certain strength, the relative movements prevent a stable settling of the particles on the separation surfaces, thus counterproductive and should be avoided during the deposition.
Für eine in bestimmten Intervallen erforderliche Matrixabreinigung stellen die vorgenannten zueinander bewegbaren Separationsflächengruppen jedoch eine signifikante Verbesserung dar.For a Matrixabreinigung required at certain intervals provide the aforementioned movable to each other Separation surface groups, however, represents a significant improvement.
Die Matrixabreinigung erfolgt vorzugsweise nach dem Gegenstromprinzip mit einem Spülfluid, wobei die Relativbewegung von mindestens zwei der vorgenannten Separationsflächenfraktionen zueinander im Spülfluid Trägheitskräfte, Zentrifugalkräfte, Turbolenzen und Scherkräfte hervorruft, welche eine Ablösung von magnetisierbaren Partikeln von den Separationsflächen auch bei noch vorhandener magnetischen Remanenz oder auch im Einfluss eines magnetischen Feldes signifikant verbessert oder auch erst nur ermöglicht.The matrix cleaning is preferably carried out according to the countercurrent principle with a flushing fluid, wherein the relative movement of at least two of the aforementioned separation surface fractions to each other in the flushing fluid causes inertial forces, centrifugal forces, turbulence and shear forces, which detachment of magnetizable particles from the separation surfaces even in the presence of magnetic remanence or in the Influence of a magnetic field significantly improved or even only possible.
Die Erfindung wird im Folgenden an Ausführungsbeispielen anhand der folgenden Figuren näher erläutert. Es zeigen
-
Fig. 1 eine prinzipielle Seitenansicht eines Ausführungsbeispiels mit Elektromagnet, -
Fig. 2 eine prinzipielle Seitenansicht eines Ausführungsbeispiels mit Permanentmagnet, -
Fig. 3 eine Schnittansicht eines Ausführungsbeispiels mit fluidisch in Serie geschalteten Separationsringscheiben, -
Fig. 4 eine Schnittansicht eines Ausführungsbeispiels mit fluidisch parallel geschalteten Separationsringscheibe sowie -
Fig. 5 eine Aufsichtdarstellung der Separationsringscheiben.
-
Fig. 1 a schematic side view of an embodiment with electromagnet, -
Fig. 2 a schematic side view of an embodiment with permanent magnet, -
Fig. 3 a sectional view of an embodiment with fluidly connected in series separation ring discs, -
Fig. 4 a sectional view of an embodiment with a fluidic parallel separation ring disc and -
Fig. 5 a top view of the Separationsringscheiben.
Wie in
Der eigentliche Hochgradienten-Magnetseparator umfasst mehrere Teileinheiten, und zwar ein im Wesentlichen zylinderförmiges Gehäuse 5, welches mit einem Deckel 6 und einem Boden 7 axial verschlossen ist. Eine Welle 8 ist konzentrisch im Gehäuse, im Ausführungsbeispiel in entsprechenden Lagerungen 9 im Deckel und / oder Boden, dichtend drehbar gelagert und über eine Kupplung 10 mit einem Antrieb 11 verbunden. Welle, Gehäuse, Deckel- und Bodenplatte bestehen aus einem unmagnetischen Werkstoff.The actual high-gradient magnetic separator comprises a plurality of subunits, namely a substantially
Kerneinheit des Hochgradienten-Magnetseparators ist die Matrix, welche sich über das vom Gehäuse 5, Deckel 6 und Boden 7 eingeschlossene Innenraumvolumen erstreckt und in dem die Abscheidung der magnetisierbaren Partikel stattfindet. Die Suspension (Fluid) mit den abzutrennenden magnetischen Partikeln tritt über den Zulauf 4 in den Hochgradienten-Magnetseparator ein und verteilt sich über den Separatorquerschnitt. Die eigentliche Abtrennung erfolgt im Bereich der Matrix an Separationsringscheiben 13 und 14. Der aufgereinigte Fluidstrom verlässt den Hochgradienten-Magnetseparator über den Ablauf 12. Zu- bzw. Ablauf bestehen aus mehreren Öffnungen im Deckel 6 bzw. Boden 7 und weisen zur besseren Strömungsverteilung jeweils eine konische Form auf.The core unit of the high-gradient magnetic separator is the matrix, which extends over the enclosed space enclosed by the
Die Matrix ist nach dem Rotor-Stator-Prinzip aufgebaut (vgl.
Die Separationsringscheiben 13 und 14, im Detail in
Die rotierenden Separationsringscheiben 14 werden über die inneren Stabilisierungsringe 17 wechselweise mit unmagnetischen inneren Abstandshülsen 18 auf die Welle 8 aufgezogen und mit einer Spannhülse 19 axial verspannt. Ebenso werden die feststehenden Separationsringscheiben 13 über die äußeren Stabilisierungsringe 16 wechselseitig mit unmagnetischen äußeren Abstandshülsen 20 in das Gehäuse 5 eingesetzt und über eine Hülse 21 verspannt. Die jeweilig nicht eingespannten inneren und äußeren Stabilisierungsringe 17 bzw. 16 bilden jeweils zu inneren bzw. äußeren Abstandshülsen 18 bzw. 20 einen Ringspalt (vgl.
Eine Matrixabreinigung erfolgt von Zeit zu Zeit vorzugsweise im Gegenstromverfahren. Als Kriterium für die Abreinigungsintervalle dient der Druckabfall im Separator, der mit der Beladung der Sedimentrationsringscheiben korreliert und bei Überschreitung eines bestimmten Wertes die Notwendigkeit der Matrixabreinigung anzeigt. Für die Matrixabreinigung wird ein Spülfluid vom Ablauf durch die Teilvolumina zum Zulauf geleitet, wobei die Welle 8 mit den rotierenden Separationsringscheiben 13 mit hoher Drehzahl (ca. 100 bis 500 U/min) gedreht werden. Durch die dabei entstehenden Scherungen in der Fluidströmung entstehen Verwirbelungen, welche die auf den Separationsringscheiben abgelagerten magnetischen Partikel mitreißen. Die separierten Partikel werden dann durch den überlagerten Spülfluidstrom aus der Matrix entfernt werden.A matrix cleaning is done from time to time, preferably in countercurrent process. The criterion for the cleaning intervals is the pressure drop in the separator, which correlates with the loading of the sedimentation ring disks and indicates the need for matrix cleaning when exceeding a certain value. For the matrix cleaning a flushing fluid is passed from the flow through the partial volumes to the inlet, the
Die Effizienz der Abreinigung lässt sich zusätzlich dadurch verbessern, dass der Hochgradienten-Magnetseparator 1 hierzu dem Einfluss eines magnetischen Feldes entzogen wird. Hierzu kann nun das Magnetfeld abgeschaltet oder der Hochgradienten-Magnetseparator aus dem Magnetfeld entfernt werden.The efficiency of the cleaning can be further improved by the fact that the high-gradient
Neben einer Rotationsbewegung kann alternativ eine Oszillationsbewegung auf die Welle 8 übertragen werden. Eine zusätzliche Kraft kann aufgebaut werden, wenn die Welle durch entsprechenden Antrieb und Lagerung zusätzlich zu einer Rotationsbewegung axial oszilliert.In addition to a rotational movement, an oscillation movement can alternatively be transmitted to the
Neben einer effizienten Abreinigungsleistung kann auch der Separationsvorgang verbessert werden, da durch Überlagern einer langsamen Rotationsbewegung während des Abscheidevorgangs die Hydrodynamik im Filter beeinflussbar ist und somit eine Strömungskanalbildung unterdrückt wird.In addition to efficient Abreinigungsleistung and the separation process can be improved because superimposed on a slow rotational movement during the deposition process, the hydrodynamics in the filter can be influenced and thus a flow channel formation is suppressed.
Der im Rahmen der Ausführungsbeispiele vorgeschlagene Aufbau der Matrix ermöglicht einen modularen und flexiblen Aufbau des Hochgradiententen-Magnetseparators. Allein durch einfachen Austausch der Abstandshülsen 18 und 20 können Anzahl und Abstand der Teilvolumina und Separationsringscheiben in einfacher Weise und gemäß eines Baukastenprinzips auch für Teilbereiche der Matrix variiert werden. Zur Minimierung des Druckverlusts ist zum Beispiel denkbar, im oberen Bereich des Hochgradienten-Magnetseparators größere Abstände zwischen den Matrixelementen zu wählen und im unteren Bereich die Matrixelemente dichter zu packen.The structure of the matrix proposed in the exemplary embodiments enables a modular and flexible construction of the high-gradient magnetic separator. Just by simply replacing the
- 11
- Hochgradienten-MagnetseparatorHigh gradient magnetic
- 22
- Magnetsystemmagnet system
- 33
- Polschuhpole
- 44
- ZulaufIntake
- 55
- Gehäusecasing
- 66
- Deckelcover
- 77
- Bodenground
- 88th
- Wellewave
- 99
- Lagerungstorage
- 1010
- Kupplungclutch
- 1111
- Antriebdrive
- 1212
- Ablaufprocedure
- 1313
- feststehende Separationsringscheibefixed separation ring disk
- 1414
- rotierende Separationsringscheiberotating separation ring disk
- 1515
- Separationsflächeseparation area
- 1616
- äußerer Stabilisierungsringouter stabilization ring
- 1717
- innerer Stabilisierungsringinner stabilization ring
- 1818
- innere Abstandshülseinner spacer sleeve
- 1919
- Spannhülseclamping sleeve
- 2020
- äußere Abstandshülseouter spacer sleeve
- 2121
- Hülseshell
- 2222
- Zulaufbohrunginlet bore
- 2323
- Ablaufbohrungdrain hole
- 2424
- Sammelkanalcollecting duct
- 2525
- doppelwandiges Gehäusedouble-walled housing
Claims (9)
- High-gradient magnetic separator (1) for the selective separation of magnetisable particles from a suspension, comprising a matrix which can be positioned in a magnet system (2) as a separation zone with at least one inlet (4, 22) and at least one outlet (12, 23) for the suspension, wherein the matrix is subdivided by plate-form magnetisable separation surfaces (15), through which the suspension can flow, into partial volumes arranged in relation to one another in rows,
characterised in that
the separation surfaces (15) are arranged alternately as fixed and moveable, wherein the moving separation surfaces are fixed on a moveably mounted carrier (8), wherein, when in operation, a relative movement of at least two of the aforesaid separation surfaces in respect of one another engenders in the flushing fluid introduced inertia forces, centrifugal forces, turbulences, and shear forces. - High-gradient magnetic separator according to claim 1, comprising a motor or actuator drive (10, 11) for the moveably mounted carrier.
- High-gradient magnetic separator according to claim 1 or 2, characterised in that the separation surfaces (15) comprise a wire fabric or a perforated metal foil or a perforated metal sheet.
- High-gradient magnetic separator according to any one of claims 1 to 3, characterised in that the carrier comprises a rotatable or laterally moveably mounted shaft (8), and the matrix and the separation surfaces (15) extend rotation symmetrically about the shaft.
- High-gradient magnetic separator according to claim 4, characterised in that the separation surfaces are part of separation ring disks (13, 14).
- High-gradient magnetic separator according to claim 4 or 5, characterised in that the matrix extends in an inner space volume of a cylindrical housing (5) with a base (7) and a cover (6), wherein at least one sealing bearing (9) for the shaft (8) is arranged in the cover or the base.
- High-gradient magnetic separator according to claim 6, characterised in that the at least one inlet and the at least one outlet are arranged exclusively in the cover (6) or in the base (7).
- High-gradient magnetic separator according to claim 6, characterised in that the housing (25) is a double-walled housing, with a collection channel (24), of which outlet holes (23) running radially inwards form the outlets, and the shaft (8) is a hollow shaft, which in the extension range of the matrix exhibits at least one radial inlet hole (22) serving as the inlet.
- High-gradient magnetic separator according to any one of the preceding claims, characterised in that at least one of the separation surfaces (15) is arranged between the at least one inlet (4, 22) and the at least one outlet (12, 23).
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DE102004034541A DE102004034541B3 (en) | 2004-07-16 | 2004-07-16 | High-gradient magnetic |
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EP1616627B1 true EP1616627B1 (en) | 2019-02-06 |
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US (1) | US7506765B2 (en) |
EP (1) | EP1616627B1 (en) |
DE (1) | DE102004034541B3 (en) |
DK (1) | DK1616627T3 (en) |
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WO2004110635A1 (en) * | 2003-06-09 | 2004-12-23 | Dow Corning Corporation | Magnetic separator apparatus |
US8075771B2 (en) * | 2005-02-17 | 2011-12-13 | E. I. Du Pont De Nemours And Company | Apparatus for magnetic field gradient enhanced centrifugation |
JP4807859B2 (en) * | 2006-01-23 | 2011-11-02 | 学校法人同志社 | Powder classifier |
EP2112957A1 (en) * | 2007-02-16 | 2009-11-04 | Koninklijke Philips Electronics N.V. | Method and separator system for separating magnetic particles, separator column for use in a separator system |
US8641899B2 (en) | 2007-05-09 | 2014-02-04 | Petroleum Specialty Rental, Llc | Method and apparatus for removing metal cuttings from an oil well drilling mud stream |
US7841475B2 (en) * | 2007-08-15 | 2010-11-30 | Kalustyan Corporation | Continuously operating machine having magnets |
US7841474B2 (en) * | 2008-11-19 | 2010-11-30 | Outotec Oyj | Beltless rare earth roll magnetic separator system and method |
US8753517B2 (en) * | 2009-05-29 | 2014-06-17 | Petroleum Specialty Rental, Llc | Method and apparatus for removing metallic matter from an oil well circulating completion fluid stream |
CN101934248B (en) * | 2009-07-01 | 2013-03-13 | 广西远健选矿工程技术研究院 | High-gradient magnetic separator of oil-cooled rotary disc |
CA2811401C (en) | 2009-10-28 | 2017-10-03 | Magnetation, Inc. | Magnetic separator |
US20120132593A1 (en) * | 2010-11-30 | 2012-05-31 | General Electric Company | Systems and methods for magnetic separation of biological materials |
AU2012245294B2 (en) | 2011-04-20 | 2015-10-29 | Magglobal, Llc | Iron ore separation device |
DE102012023382A1 (en) * | 2012-11-30 | 2014-06-18 | Hochschule Trier | Device for separating magnetic or magnetizable microparticles from a suspension by means of high-gradient magnetic separation |
CN104623965A (en) * | 2014-12-05 | 2015-05-20 | 赵宽学 | Electromagnetic iron removing machine |
CN107649287B (en) * | 2017-11-03 | 2024-04-02 | 沈阳隆基电磁科技股份有限公司 | Magnetic micro-fluidic concentrator and complete mineral processing equipment thereof |
CN109043507A (en) * | 2018-07-05 | 2018-12-21 | 镇江华大心源食品科技有限公司 | A kind of health coarse cereals composition and its production method |
AU2020246969A1 (en) * | 2019-03-27 | 2021-09-16 | Cytiva Sweden Ab | A method for separating biomolecules |
KR102348821B1 (en) * | 2021-02-24 | 2022-01-10 | 문경희 | Metal removal device of clutch type power transmission structure |
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2005
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