EP0774302B1 - Verfahren und Vorrichtung zur Trennung eines aus Feststoffpartikeln unterschiedlicher Gestalt, Grösse und/oder Dichte bestehenden Gutes in mindestens zwei Komponenten - Google Patents
Verfahren und Vorrichtung zur Trennung eines aus Feststoffpartikeln unterschiedlicher Gestalt, Grösse und/oder Dichte bestehenden Gutes in mindestens zwei Komponenten Download PDFInfo
- Publication number
- EP0774302B1 EP0774302B1 EP96118069A EP96118069A EP0774302B1 EP 0774302 B1 EP0774302 B1 EP 0774302B1 EP 96118069 A EP96118069 A EP 96118069A EP 96118069 A EP96118069 A EP 96118069A EP 0774302 B1 EP0774302 B1 EP 0774302B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- particles
- screening
- sieve
- openings
- screening openings
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/46—Constructional details of screens in general; Cleaning or heating of screens
- B07B1/4609—Constructional details of screens in general; Cleaning or heating of screens constructional details of screening surfaces or meshes
- B07B1/469—Perforated sheet-like material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/46—Constructional details of screens in general; Cleaning or heating of screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B13/00—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices
- B07B13/003—Separation of articles by differences in their geometrical form or by difference in their physical properties, e.g. elasticity, compressibility, hardness
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B4/00—Separating solids from solids by subjecting their mixture to gas currents
- B07B4/08—Separating solids from solids by subjecting their mixture to gas currents while the mixtures are supported by sieves, screens, or like mechanical elements
Definitions
- the invention relates to a method and an apparatus for Separation of solid particles of different shapes, Size and / or density of existing goods in at least two Components according to the preamble of claims 1 and 6 respectively.
- a variety of methods and devices are known those for the separation of solid particles according to certain differentiation criteria be used. For example, find Vibrating sieves and separation processes using vibrating sieves already at the classification, i.e. when separating a good in different grain sizes, use, the of which Vibratory drives vibrations introduced into the sieve bottom one serve to throw the particles up to repeat them close to the sieve openings and secondly to the particles in horizontal or slightly inclined sieve trays to be transported from the task to the discharge by micro-throws.
- the particles are known vibrating screens excited in the same way by the vibrating drive one vertically upwards away from the sieve plate and the other in Direction of transport, i.e. in the direction from task to Discharge, accelerated.
- DE-AS 1 193 345 describes a method and a device known for the classification of difficult screenings. That there disclosed vibrating screen has a lower, more inclined Section and an upper, more steeply inclined section on and is alternately excitable and opposite, which means that opposite excitation on the steeper inclined section for the most part consisting of Unterkorn and Stahlkorn of the good is moving upwards, while the excitement is constant it is avoided that unscreened material leaves the vibrating screen.
- the separation of a good into two or more components is mostly associated with difficulties when the to separating components from each other only slightly, for example the same or similar physical properties and have comparable dimensions, such as Mixed shredded plastic waste almost the same density as recycling plastic parts of motor vehicles or plastic housings from electrical or electronic devices.
- These platelet or disc-shaped snippets differ in essential only in terms of their thickness, this difference in thickness often with different material properties is linked, due to the previous purpose of the Plastics.
- the separation of such a good with the help of a Air cooker is in processing technology 36 (1995) No. 7 p. 314-320 described, but this known method none large throughputs allowed.
- a separation of platelets of different thicknesses or disc-shaped particles by sieving is known with Vibrating sieves, their sieve openings in the plane of the sieve bottom are arranged, not possible because platelet or disk-shaped particles predominantly in their most stable position move on the sieve bottom, in which they lay flat on the The sieve bottom rests, so that all the particles Screen openings face their broad sides.
- For classifying tobacco leaf parts is from DE-OS 35 05 502 already a sieve with an inclined sieve bottom and a vibration exciter known per se, in which the Sieve openings between two up or down over the Protruding protrusions are arranged so that they are too open diagonally upwards.
- the good is there through the Vibrations of the vibrating screen from one at the lower end of the Sieve bottom arranged task to one at its upper end ordered discharge transported.
- the over the top bulges Pieces of tobacco leaf transported away either fall directly into the screen openings or on the bevels arranged in front of them the lower bulges, whereby only the tobacco leaves through the Sieve openings fall, whose dimensions are smaller than that Hole width is the same. Thickness sorting is with the known classification device not possible.
- a vibrating sieve device is already known from US-A-4,351,719 for separating wood chips on the one hand and over and Undersize on the other hand with the features of the generic term of Claim 6 known, in which the acceleration of the Particle against the direction of transport serves the Extend the dwell time of the coarser particles on the sieve, until the entire undersize is separated.
- the invention is based on the object Process and an apparatus of the type mentioned in the foregoing to improve that they're not just separating one from flat solid particles existing after the Allow particle thickness but also according to the particle density.
- the method according to the invention is characterized by this from that the sieve openings from below with an air flow are applied while the device according to the invention by means of loading the sieve openings of is marked below with an air flow.
- the invention takes advantage of the fact that the particles be aligned before entering the sieve openings that their front or narrow side surfaces always flow against become. Because the relationship between slope downforce on the one hand and aerodynamic drag on the other hand in the specific heavier particles are larger, they slide or fall against the air flow into the sieve openings, while the specifically lighter particles are blown upwards.
- a transport direction of the material to be sieved from above below and a vibratory drive with an upward, vibration component opposite to the transport direction causes the flake, disc or rotate platelet-shaped particles in the course of the micro-throws and repeated with their front or narrow side surfaces in the direction the sieve openings are aligned, the opening width so is chosen that only those particles pass through, at which the dimensions of the front or narrow side surface falls below the predetermined value, in other words the thinner particles.
- the particles can thus be placed in one in front of the sieve openings Align position in which a separation of two components Shape properties is possible.
- this is done Throwing back the particles in the method according to the invention in that the vibrations of the sieve plate cause forces in the particles are introduced, which consist of two Assemble power components, one of which is vertical to the sieve bottom and the other parallel to Sieve bottom in an opposite to the transport direction Direction points so that a single, unobstructed on the Particle lying on the sieve floor along a parabolic path thrown up towards the task.
- the inclination of the Sieve bottom chosen relatively steep, so that the slope downforce despite the opposing force component due to the vibratory drive a transport of the screenings towards the discharge causes.
- the inclination of the screen openings at an angle to Sieve plate level and its orientation towards the task facilitates the entry of the thinner particles into the Sieve openings, as a result of the micro-throws on the sieve bottom particles hitting above the sieve openings on the Slide the sieve bottom down towards the sieve openings, with their broad sides on the sieve bottom rest and their front or narrow side surfaces in the direction of the sieve openings. While the thicker particles oppose push the edge of the sieve openings and through the Vibration movement of the sieve bottom opposite to Direction of transport, i.e.
- Another advantage of loading the screen openings with air is that it is a fluidized form Particle bed causes on the sieve bottom, so that the turbulent movement of the particles is calmed.
- sieve openings which are inclined with respect to the sieve plate level the airflow emerging from the sieve openings a certain braking of the material to be screened, so that the particles more often in front of the screen openings on their way to discharge reach.
- an extractor hood arranged above the sieve bottom the air flow can also be used to remove dusty components from coarse screenings, such as abrasion to dissipate upwards.
- a particularly good separation effect can be achieved e.g.
- the slot-shaped sieve openings between each two adjacent angle bars arranged one of which A plurality arranged one behind the other transversely to the transport direction and forms the step-shaped sieve bottom in longitudinal section.
- the angle strips essentially consist of two legs, their tops towards the task or towards of the discharge point, the feed-side leg is usually narrower than the discharge side leg.
- the two legs make a right or acute angle one that opens towards the sieve bottom.
- the method according to the invention and the device according to the invention enable the processing of large quantities of a Good thing that consists of a main component intended for use and one or more, in much less There are quantities of foreign substance components present with Using the invention quickly, effectively and practically completely can be separated.
- the screen separating device 1 shown in FIG. 1 is intended for this purpose are used, mainly from dried Onion flakes as the first component of existing screenings of small amounts of impurities as a second component to separate that inadvertently during manufacture Screenings have gotten.
- the impurities include thin glass fragments, especially thin lamp glass fragments, the hover speeds similar to those in the air classifier Part of the onion flakes has a similar color as they possess, so that they cannot be have it separated by a color sorter.
- the impurities are small stones, lumps of clay or Plastic particles, the weight of which is also only insignificant differs from that of the smaller onion particles, whereby their dimensions are essentially the dimensions of the smallest Face or narrow faces of part of the onion flakes correspond.
- the screen separator 1 consists essentially of a Vibrating screen 2, comprising one at an angle to the horizontal inclined sieve plate 4 with a plurality of sieve openings 6, one arranged at the upper end of the vibrating screen 2 Feed hopper 8 with a metering device for the dosed feeding of the screenings onto the upper end of the screen bottom 4, one at the lower end of the vibrating screen 2 or Sieve bottom 4 arranged discharge 10 for the first component of the screened material, one arranged below the discharge 10 Conveyor belt 12 for removing this component, one below the sieve bottom 4 arranged sump 16 for the through the screen openings 6 falling second component, and one Vibratory drive 18, which is coupled to the vibrating screen 2, to set the sieve plate 4 in vibration.
- the vibrating screen 2 can, as shown in Fig. 1, as positively guided linear vibrating screen can be formed, alternatively however, this also includes the use of vibrating screens an elliptical oscillation movement possible.
- the vibration system which is a two-mass vibration system can be formed, as shown in Fig. 1, but also in the form of a one-mass vibration system can be used.
- the frequency of the vibrations of the oscillating drive 18 expediently in a range of 3 to 20 Hz and preferably 5 to 7 Hz, is Amplitude depending on the oscillation frequency and the Screen material between about 5 mm at high frequency and screen material with small particle size and about 40 mm at low frequency and coarser screenings so that the particles have time to settle in front of the sieve openings 6 so that their front or narrow side surfaces are facing.
- the vibrating screen comprises 2 shows a fixed rigid frame shown in simplified form 20 with three vertical arms 22, on their free upper At the end of a double rocker arm 24 is rotatably mounted, the upper end 26 articulated with the sieve bottom 4 supporting box-shaped collecting pan 16 is connected, which together form the first mass, while its lower end 30 also articulated with a counterweight 32 forming the second mass is connected, the oscillation movement of the oscillation movement is opposite to the first mass.
- the Vibrating drive 18 of the vibrating screen 2 comprises in the illustrated Embodiment an electric motor 36, the output shaft via a belt drive 38 with a rotatably mounted Flywheel 40 is connected, via which a crank pin 42 eccentrically protrudes, which is articulated with the lower one End of a push rod 44 is connected, the upper end articulated via a pivot joint 46 to the collecting trough 16 is.
- balancing drives can also be used or magnetic drives are used, but independently on the choice of the drive common to all vibrating screens is that they are excited in opposite directions, i.e.
- Main vibration direction X with a parallel to the sieve plate 4 Transport direction T from task 8 to discharge 10 one Includes angle ⁇ of more than 90 degrees.
- angle ⁇ of more than 90 degrees.
- main swing direction was chosen because the direction of movement of the sieve plate in the course of a upward half-vibration can change. In which linear oscillator shown, this change results by the eccentric arrangement of the crank pin 42, the main swing direction X through the center of the flywheel 40 and the axis of rotation of the swivel joint 46 extends.
- Such an arrangement of the oscillating drive 18 has the consequence that due to its vibration exciter in the Vibrating sieve 2 vibrations initiated acceleration forces K0 can be exercised on the screenings, which consist of two Assemble power components K1 and K2, one of which (K1) perpendicular to the sieve plate 4 and the other (K2) parallel to the sieve plate 4 in a direction of transport T. points in the opposite direction.
- the one arranged over the drip pan 16 of the screen separating device 1 Sieve plate 4 can be made of stamped and deformed sheet steel 48 with hump-shaped projections 50, which after above to the steel sheet lying in the sieve plate level E. 48 survive and on her towards task 8 Side or flank to form the screen openings 6 open are. While the closed in the direction of the discharge 10 The protrusions 50 side is relatively flat to the one Projections 50 connecting flat section 52 of the sieve bottom 4 falls, the sieve opening 6 is from a feed side Punching edge 54 of the projections 50 enclosed in the illustrated Embodiment at an angle of 90 degrees the flat part 52 of the sieve bottom plate 48 inclined is.
- the width b of the slot-shaped screen openings 6 is selected that all particles of the second component with their smaller forehead or in the direction of transport Narrow side surfaces essentially parallel to the sieve plate level can pass through the screen openings 6 if they in their most stable position, i.e. parallel to the sieve plate level E aligned broad side surfaces, through the screen openings 6 fit.
- the sieve bottom 4 can also be designed as in 4 and 5, where the projections 50 on the discharge side steadily up to the staggered below and behind arranged screen openings 6 in the adjacent projections 50 fall off, so that each above the sieve openings 6 arranged surface areas 60 of the sieve plate 4 steeper are inclined and thus the particles slide through them Promote component through the screen openings 6.
- the Sieve openings 6 are here also to the Sieve openings 6 towards falling edges of the projections 50 so shaped that the impacting solid particles to the screen openings 6 be directed.
- FIG. 6 and 7 Another particularly advantageous embodiment of a Sieve plate 4 is shown in Figures 6 and 7.
- the screen openings 6 each between two parallel ones
- Angle strips 55 arranged transversely to the transport direction T, i.e. in the horizontal direction over at least one Part and preferably over the entire width of the sieve plate 4 extend.
- the angle strips 55 can, depending on the material to be screened Aluminum, a resistant and abrasion-resistant plastic or other suitable material.
- angular strips arranged one behind the other 55 each have two legs 51 and 53, which are different are wide, the narrower legs 53 on the feed side are arranged and only about half as wide as that discharge leg 51 are.
- the two legs 51, 53 each angle bar 55 close an acute or right An angle ⁇ , which extends to the underside of the sieve plate 4 opens.
- the slot-shaped sieve openings 6 are located in each case between the free ends of the legs 51, 53 adjacent Angle strips 55, on the one hand by the for Discharge 10 facing top of the leg 51 and on the other hand by a parallel to the top of the leg 51, in Distance from this arranged end face of the task side Leg 53 are limited.
- the opening width is b generally set so that all particles of the sieved second component with its front or narrow side surface fit through the sieve openings 6.
- the sieve openings are designed so that they are essentially perpendicular to the above the screen openings arranged surfaces of the sieve plate, i.e. your The direction of passage is essentially parallel to these surfaces and parallel or at an acute angle to the sieve plate level aligned, with the sieve openings in vertical Top view of the sieve plate level are not visible and therefore have no pass component in this direction.
- the cut onion flakes are partly the same thickness like the larger stones or other foreign bodies of the first Component can, which is under the sieve bottom 4th arranged drip pan 16 via a supply line, not shown pressurized with compressed air, which as a result of the loading of screenings evenly distributed through the sieve openings 6 flows upwards and there is a wind sifting through the Sieve openings 6 passing particles of the first and second component causes.
- Opening width b of the sieve openings selected so that only the thinner particles of the component to be screened with their Front or narrow side surfaces through the screen openings 6 fit through, but not the thicker particles of the to be discharged Component, while in a combined thickness and density separation is such that the thinner and at the same time, specifically heavier particles of the sieved Component and the thinner particles of the to be discharged Fit component, with the passage of the latter prevented by the air flow in the screen openings 6 becomes.
- the air supply to the sump 16 is when the sieving material set at the beginning so that the flow rate in the sieve openings 6 between 5 and 10 m / s and preferably about 7 and 9 m / s.
- Removing the screened second component from the with Compressed air collecting tray 16 can for example via a lock, not shown.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Combined Means For Separation Of Solids (AREA)
Description
- Fig. 1:
- eine teilweise geschnittene schematische Seitenansicht einer erfindungsgemäßen Siebtrennvorrichtung;
- Fig. 2:
- eine Draufsicht auf einen Teil eines Siebbodens der Vorrichtung;
- Fig. 3a:
- einen Längsschnitt durch den Siebbodenteil aus Fig. 2 entlang der Linie 3a - 3a;
- Fig. 3b:
- einen Schnitt durch den Siebbodenteil aus Fig. 2 entlang der Linie 3b - 3b;
- Fig. 4:
- eine Draufsicht auf einen Teil eines anderen Siebbodens;
- Fig. 5:
- einen Längsschnitt durch den Siebbodenteil aus Fig. 4 entlang der Linie 5 - 5;
- Fig. 6:
- eine Draufsicht auf einen Teil eines Siebbodens mit spaltförmigen Sieböffnungen;
- Fig. 7:
- einen Längsschnitt durch den Siebbodenteil aus Fig. 7 entlang der Linie 7 - 7.
Claims (9)
- Verfahren zur Trennung eines aus Feststoffpartikeln unterschiedlicher Gestalt, Größe und/oder Dichte bestehenden Gutes in mindestens zwei Komponenten, bei dem das Gut über einen gegenüber der Horizontalen geneigten Siebboden (4) eines in Schwingungen versetzten Schwingsiebs (2) nach unten transportiert wird, wobei ein Teil der Partikel durch die Schwingungen in einer zur Transportrichtung (T) entgegengesetzten Richtung beschleunigt wird und die Partikel der einen Komponente am unteren Ende des Siebbodens ausgetragen werden und die Partikel der anderen Komponente durch Sieböffnungen (6) des Siebbodens (4) hindurch ausgesiebt werden, wobei ein Gut mit unterschiedlich dicken flocken-, scheiben- oder plättchenförmigen flächigen Partikeln aufgegeben wird, welche durch die Schwingungen des Schwingsiebs (2) mit ihren Stirn- oder Schmalseitenflächen vor die unter einem Winkel zur Siebbodenebene (E) geneigten schlitzförmigen Sieböffnungen (6) ausgerichtet werden, deren Öffnungsweite (b) so bemessen ist, dass nur diejenigen Partikel durch die Sieböffnungen (6) hindurchpassen, deren Dicke einen vorgegebenen Wert unterschreitet, dadurch gekennzeichnet, dass die Sieböffnungen (6) von unten her mit einem Luftstrom beaufschlagt werden.
- Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass der Luftstrom durch die Sieböffnungen (6) mindestens teilweise in eine zur Transportrichtung (T) entgegengesetzte Richtung gelenkt wird.
- Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass eine Strömungsmenge des Luftstroms so eingestellt wird, dass mindestens ein Teil des Gutes auf dem Siebboden (4) fluidisiert wird.
- Verfahren nach einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, dass eine Strömungsgeschwindigkeit des Luftstroms in den Sieböffnungen (6) so eingestellt wird, dass von den durch die Sieböffnungen (6) hindurchpassenden Partikeln des Gutes im wesentlichen nur diejenigen durch die Sieböffnungen (6) hindurchtreten, deren spezifisches Gewicht über einem vorbestimmten Wert liegt.
- Verfahren nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, dass als Gut getrocknete Früchte oder Gemüse oder andere im wesentlichen trockene oder getrocknete Lebensmittel eingesetzt werden, welche in geringen Mengen abzutrennende Fremdstoffpartikel enthalten, deren Dicke und ggf. Dichte sich von derjenigen der Lebensmittel unterscheidet.
- Vorrichtung zur Trennung eines aus Feststoffpartikeln unterschiedlicher Gestalt, Größe und/oder Dichte bestehenden Gutes, das unterschiedlich dicke flocken-, scheiben- oder plättchenförmige flächige Partikel enthält, in mindestens zwei Komponenten, umfassend mindestens ein Schwingsieb (2) mit einem mit Sieböffnungen (6) versehenen und gegenüber der Horizontalen geneigten Siebboden (4), der schlitzförmige und unter einem Winkel zur Siebbodenebene (E) geneigte Sieböffnungen (6) aufweist, eine im Bereich eines oberen Endes des Schwingsiebs (2) angeordnete Gutaufgabe (8), einen am unteren Ende des Schwingsiebs angeordneten Austrag (10) für die eine Komponente, eine unterhalb des Siebbodens (4) angeordnete Auffangeinrichtung (16) für die andere Komponente, einen mit dem Siebboden (4) gekoppelten Schwingantrieb (18), der einen Teil der Partikel in einer zur Transportrichtung entgegengesetzten Richtung beschleunigt, so dass die Partikel mit ihren Stirn- oder Schmalseitenflächen vor den Sieböffnungen (6) ausgerichtet werden und diejenigen Partikel durch die Sieböffnungen (6) hindurchtreten, deren Dicke kleiner ist als die Öffnungsweite (b) der Sieböffnungen, gekennzeichnet durch Einrichtungen zum Beaufschlagen der Sieböffnungen (6) von unten her mit einem Luftstrom.
- Vorrichtung nach Anspruch 6, dadurch gekennzeichnet, dass eine Strömungsgeschwindigkeit des Luftstroms in den Sieböffnungen (6) so einstellbar ist, dass von den durch die Sieböffnungen (6) hindurchpassenden Partikeln des Gutes im wesentlichen nur diejenigen durch die Sieböffnungen (6) hindurchtreten, deren spezifisches Gewicht einen vorbestimmten Wert übersteigt.
- Vorrichtung nach Anspruch 6 oder 7, dadurch gekennzeichnet, dass der Siebboden (4) unter einem Winkel α von 20 bis 45 Grad gegenüber der Horizontalen geneigt ist.
- Vorrichtung nach einem der Ansprüche 6 bis 8, dadurch gekennzeichnet, dass die Sieböffnungen (6) jeweils zwischen zwei Schenkeln (51, 53) zweier benachbarter Winkelleisten (55) angeordnet sind, welche parallel zueinander und quer zur Transportrichtung (T) verlaufen.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19542688A DE19542688A1 (de) | 1995-11-16 | 1995-11-16 | Verfahren und Vorrichtung zur Trennung eines aus Feststoffpartikeln unterschiedlicher Gestalt, Größe und/oder Dichte bestehenden Gutes in mindestens zwei Komponenten |
DE19542688 | 1995-11-16 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0774302A1 EP0774302A1 (de) | 1997-05-21 |
EP0774302B1 true EP0774302B1 (de) | 2001-06-27 |
Family
ID=7777595
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96118069A Expired - Lifetime EP0774302B1 (de) | 1995-11-16 | 1996-11-12 | Verfahren und Vorrichtung zur Trennung eines aus Feststoffpartikeln unterschiedlicher Gestalt, Grösse und/oder Dichte bestehenden Gutes in mindestens zwei Komponenten |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0774302B1 (de) |
AT (1) | ATE202506T1 (de) |
DE (2) | DE19542688A1 (de) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19717514A1 (de) * | 1997-04-25 | 1998-10-29 | Peter Dieckmann | Verfahren und Vorrichtung zur Aufbereitung von getrockneten Kräutern |
CN1473193A (zh) * | 2000-10-31 | 2004-02-04 | 宝洁公司 | 洗涤剂片剂的再混合 |
EP2272595A1 (de) | 2009-07-09 | 2011-01-12 | Lubo Screening- & Recyclingsystems B.V. | Abfallverarbeitung |
PL232751B1 (pl) * | 2013-08-12 | 2019-07-31 | Int Tobacco Machinery Poland Spolka Z Ograniczona Odpowiedzialnoscia | Zespół do oddzielania i sposób oddzielania wybranych obiektów wadliwych z grupy obiektów stosowanych w przemyśle tytoniowym |
CN112845065B (zh) * | 2021-02-23 | 2022-04-12 | 迁安市强达铁选有限公司 | 一种高频振动筛 |
CN112934709A (zh) * | 2021-04-19 | 2021-06-11 | 包观秀 | 一种对不同厚度金刚石刀头进行分拣的装置 |
CN115722436A (zh) * | 2021-08-26 | 2023-03-03 | 广州达安基因股份有限公司 | 物料球筛选装置 |
CN114405809B (zh) * | 2021-12-28 | 2023-02-17 | 盐城健牌科技有限公司 | 一种具有防尘功能的汽车密封条颗粒料振动分筛装置 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1193345B (de) * | 1962-06-28 | 1965-05-20 | Fraembs & Freudenberg K G | Vibrationssiebflaechen |
US4351719A (en) * | 1981-02-19 | 1982-09-28 | Morbark Industries, Inc. | Vibrating screen apparatus |
DE3505502A1 (de) | 1985-02-16 | 1986-08-21 | Wilh. Quester Maschinenfabrik GmbH, 5030 Hürth | Tabak-klassiervorrichtung |
US4802591A (en) * | 1986-08-29 | 1989-02-07 | Rotex, Inc. | Louvered chip screener |
JP3070173B2 (ja) * | 1991-08-21 | 2000-07-24 | 神鋼電機株式会社 | 振動ふるい装置 |
JP3160953B2 (ja) * | 1991-08-30 | 2001-04-25 | 神鋼電機株式会社 | 振動ふるい装置 |
-
1995
- 1995-11-16 DE DE19542688A patent/DE19542688A1/de not_active Withdrawn
-
1996
- 1996-11-12 EP EP96118069A patent/EP0774302B1/de not_active Expired - Lifetime
- 1996-11-12 DE DE59607163T patent/DE59607163D1/de not_active Expired - Fee Related
- 1996-11-12 AT AT96118069T patent/ATE202506T1/de not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
DE19542688A1 (de) | 1997-05-22 |
ATE202506T1 (de) | 2001-07-15 |
EP0774302A1 (de) | 1997-05-21 |
DE59607163D1 (de) | 2001-08-02 |
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