EP0223639A1 - Method of and device for putting apart spherical materials possibly showing imperfections - Google Patents
Method of and device for putting apart spherical materials possibly showing imperfections Download PDFInfo
- Publication number
- EP0223639A1 EP0223639A1 EP86402142A EP86402142A EP0223639A1 EP 0223639 A1 EP0223639 A1 EP 0223639A1 EP 86402142 A EP86402142 A EP 86402142A EP 86402142 A EP86402142 A EP 86402142A EP 0223639 A1 EP0223639 A1 EP 0223639A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- turn
- balls
- pitch
- broken
- steps
- 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
- 239000000463 material Substances 0.000 title claims abstract description 9
- 238000000034 method Methods 0.000 title claims abstract 5
- 239000002245 particle Substances 0.000 claims abstract description 15
- 239000000203 mixture Substances 0.000 claims description 10
- 239000007787 solid Substances 0.000 claims description 10
- 239000003973 paint Substances 0.000 claims description 3
- 239000004033 plastic Substances 0.000 claims description 2
- 238000005204 segregation Methods 0.000 claims description 2
- 230000037361 pathway Effects 0.000 claims 1
- 230000000630 rising effect Effects 0.000 claims 1
- 239000008247 solid mixture Substances 0.000 claims 1
- 239000011324 bead Substances 0.000 abstract description 10
- 238000000926 separation method Methods 0.000 abstract description 6
- 230000001174 ascending effect Effects 0.000 abstract 1
- 239000008187 granular material Substances 0.000 abstract 1
- 235000013339 cereals Nutrition 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 2
- 239000012798 spherical particle Substances 0.000 description 2
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000008298 dragée Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 239000011214 refractory ceramic Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000001612 separation test Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Images
Classifications
-
- 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
- B07B13/10—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects
- B07B13/11—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects involving travel of particles over surfaces which separate by centrifugal force or by relative friction between particles and such surfaces, e.g. helical sorters
Definitions
- the present invention relates to a helical vibrating lifting device and its use for effecting an effective separation between spherical particles and non-spherical particles, for example for separating balls of neighboring sizes, some being round, the others being broken (broken).
- This invention possibly coupled with separation by screening, makes it possible in particular to restore to refiners or petrochemicals batches of inert perfectly calibrated beads.
- the device according to the invention can be used for other applications, for example, for separating the shell grains in the food industry or for separating spherical catalysts from poorly formed spheres.
- the apparatus makes it possible to carry out the separation of spherical materials according to their size as well as the separation of the spheres and of the fragments of spheres which will be called hereinafter "broken".
- the system according to the invention makes it possible to exclude broken grains from a mixture of spherical or ovoid products and, for example, to eliminate broken ceramic beads in beds of inert beads which refiners have in hydrotreatment reactors which allows, after sorting, to restore a batch of inert balls perfectly calibrated and therefore reusable with an efficiency equal to that of new materials.
- the apparatus according to the invention is of the helical vibrating lift type; it consists of at least one substantially horizontal turn (substantially vertical axis) whose width is between approximately 50 and 400mm and preferably between 200 and 300mm with a pitch (distance between the tops of two turns) from 50 to 150mm, and preferably of the order of 80 to 120mm, for example around 100mm.
- the slope is from 2 to 20 degrees approximately and preferably from 9 to 16 degrees.
- the turn or each turn, if there are several, has 2 to 9 steps or more for example up to 150 steps by way of example and is wound around a hollow barrel at the base or at the top of which, for example, systems are arranged allowing the barrel-turn assembly to take a vibratory movement of variable amplitude.
- the vibrations can be produced by at least one system placed at any suitable level, for example at the base or at the top of the barrel or else positioned around the coil.
- the unbalance motors the electro-magnetic vibrators (excited by a variable cycle, with creation of pulses), and the unbalance exciters.
- the amplitude (lateral) of the vibration movement thus communicated to the assembly can thus vary between 0.2 and 15mm and preferably between 2 and 5.5mm.
- the barrel-turn assembly, source of vibration could be arranged, for example, on a central post serving as support, various anti-vibration materials which can be interposed between the barrel and the post.
- the material used for making the coil, or more exactly the steps of the coil may be a blasted mild steel, or a stainless steel, etc., coated with an anti-rust paint.
- modifying the coating of the pitch that is to say, for example, by spraying a plastic paint or by sticking a rubber band, or any other suitable material, it is possible on the one hand to modify the coefficient of adhesion and, therefore, the segregation of powdery products for a given amplitude, but also considerably reduce the noise caused by the movements of balls on the steel.
- Figure 1 there is shown a barrel or post (7) with a turn (4) to 5 steps, such as (5).
- the unbalance motor (6) generates vibrations around the axis or post.
- the flow of the mixture of beads to be separated or of beads and broken pieces to be separated is introduced via the pipe. 1 into the periphery of the coil, in a step between the upper step and the lower step, and for example in a step located halfway up the coil.
- the solid particles will thus circulate on the band of the turn or circulation band of the step, this circulation band being delimited by the internal and external edges of each step.
- the larger balls they descend along the whorl, with a speed which accelerates so that under the effect of centrifugal force, the large balls roll more and more on the periphery of the whorl, c that is to say mainly between the outer edges of the circulation band of each step and said middle part of the step. Therefore, gradually and without hindering, the balls descend along the outer edges of the steps of the turn against small beads or broken pieces that travel from bottom to top, along the inner edges of the steps of the turn.
- the vibration system is subject to an appropriate adjustment depending on the nature and dimensions of the particles to be withdrawn.
- the small balls or the broken pieces are evacuated at the top by the pipe 3, the balls of the desired size being recovered by the pipe 2 at the bottom of the turn.
- FIG. 1 shows the apparatus of Figure 1, seen from above.
- Each of these 3 types of particles represents 1/3 by volume of the total mixture.
- the amplitude of the vibrations was adjusted to 2mm: it was observed that the breaks are animated by a vibration movement such that, by successive micro-projection on the step, they rise in the coil and leave the coil via the conduit 3 while the balls of diameters 2.54cm and 1.27cm descend downwards or remain in the lower part of the coil, and end up being evacuated through the conduit 2.
Landscapes
- Combined Means For Separation Of Solids (AREA)
- Crushing And Grinding (AREA)
Abstract
L'invention concerne un procédé et un appareillage pour la séparation de matières pulvérulentes, sous forme de billes ou de granulés. Elle est caractérisée par l'emploi d'un élévateur vibrant hélicoïdal (4) soumis à des vibrations dont l'amplitude est choisie de façon à provoquer sur les pas (5) de la spire la circulation ascendante des particules dont on veut se débarrasser, en maintenant la descente vers le bas de la spire des particules à récupérer. L'invention permet notamment de séparer des billes rondes de billes cassées.The invention relates to a method and an apparatus for the separation of pulverulent materials, in the form of beads or granules. It is characterized by the use of a helical vibrating elevator (4) subjected to vibrations the amplitude of which is chosen so as to cause on the steps (5) of the turn the ascending circulation of the particles which one wishes to get rid of, maintaining the descent to the bottom of the turn of the particles to be recovered. The invention makes it possible in particular to separate round balls from broken balls.
Description
La présente invention concerne un appareil élévateur vibrant hélicoïdal et son utilisation pour effectuer une séparation efficace entre des particules sphériques et des particules non sphériques, par exemple pour séparer des billes de tailles voisines les unes étant rondes, les autres étant cassées (brisures).The present invention relates to a helical vibrating lifting device and its use for effecting an effective separation between spherical particles and non-spherical particles, for example for separating balls of neighboring sizes, some being round, the others being broken (broken).
Cette invention, couplée éventuellement à la séparation par criblage, permet notamment de restituer aux raffineurs ou aux pétrochimistes des lots de billes inertes parfaitement calibrées.This invention, possibly coupled with separation by screening, makes it possible in particular to restore to refiners or petrochemicals batches of inert perfectly calibrated beads.
Mais l'appareil selon l'invention peut être utilisé pour d'autres applications, par exemple, pour séparer les grains de coques en agro-alimentaire ou pour séparer des catalyseurs sphériques d'avec des sphères mal formées.However, the device according to the invention can be used for other applications, for example, for separating the shell grains in the food industry or for separating spherical catalysts from poorly formed spheres.
D'une façon générale, l'appareil permet de réaliser la séparation de matériaux sphériques suivant leur taille ainsi que la séparation des sphères et des éclats de sphères qu'on appellera ci-après "brisures".Generally, the apparatus makes it possible to carry out the separation of spherical materials according to their size as well as the separation of the spheres and of the fragments of spheres which will be called hereinafter "broken".
Le système selon l'invention permet d'exclure les brisures d'un mélange de produits sphériques ou ovoïdes et, par exemple, d'éliminer les billes de céramiques cassées dans des lits de billes inertes que les raffineurs disposent dans les réacteurs d'hydrotraitement ce qui permet, après triage, de restituer un lot de billes inertes parfaitement calibrées et donc réutilisables avec une efficacité égale à celle des matériaux neufs.The system according to the invention makes it possible to exclude broken grains from a mixture of spherical or ovoid products and, for example, to eliminate broken ceramic beads in beds of inert beads which refiners have in hydrotreatment reactors which allows, after sorting, to restore a batch of inert balls perfectly calibrated and therefore reusable with an efficiency equal to that of new materials.
L'appareil selon l'invention est du type élévateur vibrant hélicoïdal ; il est constitué d'au moins une spire sensiblement horizontale (axe sensiblement vertical) dont la largeur est comprise entre environ 50 et 400mm et de préférence entre 200 et 300mm avec un pas (distance entre les sommets de deux spires) de 50 à 150mm, et de préférence de l'ordre de 80 à 120mm, par exemple environ 100mm. La pente est de 2 à 20 degrés environ et de préférence de 9 à 16 degrés. La spire ou chaque spire, s'il y en a plusieurs, comporte 2 à 9 pas ou davantage par exemple jusqu'à 150 pas à titre d'exemple et est enroulée autour d'un fût creux à la base ou au sommet duquel, par exemple, sont disposés des systèmes permettant à l'ensemble fût-spire de prendre un mouvement vibratoire d'amplitude variable.The apparatus according to the invention is of the helical vibrating lift type; it consists of at least one substantially horizontal turn (substantially vertical axis) whose width is between approximately 50 and 400mm and preferably between 200 and 300mm with a pitch (distance between the tops of two turns) from 50 to 150mm, and preferably of the order of 80 to 120mm, for example around 100mm. The slope is from 2 to 20 degrees approximately and preferably from 9 to 16 degrees. The turn or each turn, if there are several, has 2 to 9 steps or more for example up to 150 steps by way of example and is wound around a hollow barrel at the base or at the top of which, for example, systems are arranged allowing the barrel-turn assembly to take a vibratory movement of variable amplitude.
Les vibrations peuvent être produites par au moins un système placé à tout niveau adéquat, par exemple à la base ou au sommet du fût ou encore positionné autour de la spire. Parmi les systèmes que l'on pourra choisir, on nommera par exemple : les moteurs à balourds, les vibrants électro-magnétiques (excités par un cycle variable, avec création d'impulsions), et les excitatrices à balourds. L'amplitude (latérale) du mouvement de vibration ainsi communiqué à l'ensemble (déplacement latéral des parois verticales du fût) peut ainsi varier entre 0,2 et 15mm et de préférence entre 2 et 5,5mm. L'ensemble fût-spire, source de vibration, pourraît être disposée, à titre d'exemple, sur un poteau central servant de support, divers matériaux anti-vibratiles pouvant être interposés entre le fût et le poteau. Le matériau utilisé pour la confection de la spire, ou plus exactement des pas de la spire, peut être un acier doux sablé, ou un inox, etc..., revêtue d'une peinture anti-rouille. En modifiant le revêtement du pas, c'est-à-dire, par exemple, en projetant une peinture plastique ou en collant une bande caoutchouc, ou toute autre matière convenable, on peut d'une part modifier le coefficient d'adhérence et, par conséquent, la ségrégation des produits pulvérulents pour une amplitude donnée, mais aussi réduire considérablement le bruit provoqué par les mouvements de billes sur l'acier.The vibrations can be produced by at least one system placed at any suitable level, for example at the base or at the top of the barrel or else positioned around the coil. Among the systems which one will be able to choose, one will name for example: the unbalance motors, the electro-magnetic vibrators (excited by a variable cycle, with creation of pulses), and the unbalance exciters. The amplitude (lateral) of the vibration movement thus communicated to the assembly (lateral displacement of the vertical walls of the barrel) can thus vary between 0.2 and 15mm and preferably between 2 and 5.5mm. The barrel-turn assembly, source of vibration, could be arranged, for example, on a central post serving as support, various anti-vibration materials which can be interposed between the barrel and the post. The material used for making the coil, or more exactly the steps of the coil, may be a blasted mild steel, or a stainless steel, etc., coated with an anti-rust paint. By modifying the coating of the pitch, that is to say, for example, by spraying a plastic paint or by sticking a rubber band, or any other suitable material, it is possible on the one hand to modify the coefficient of adhesion and, therefore, the segregation of powdery products for a given amplitude, but also considerably reduce the noise caused by the movements of balls on the steel.
Sur la figure 1 on a représenté un fût ou poteau (7) avec une spire (4) à 5 pas, tels que (5).In Figure 1 there is shown a barrel or post (7) with a turn (4) to 5 steps, such as (5).
Le moteur à balourds (6), engendre les vibrations autour de l'axe ou poteau .The unbalance motor (6) generates vibrations around the axis or post.
Le flux du mélange de billes à séparer ou de billes et brisures à séparer (céréales, céramiques réfractaires, pastilles, dragées utilisées en pharmacie, confiserie, catalyseurs, etc... est introduit par la conduite.1 dans la périphérie de la spire, dans un pas situé entre le pas supérieur et le pas inférieur, et par exemple dans un pas situé à mi-hauteur de la spire.The flow of the mixture of beads to be separated or of beads and broken pieces to be separated (cereals, refractory ceramics, pellets, dragees used in pharmacy, confectionery, catalysts, etc.) is introduced via the pipe. 1 into the periphery of the coil, in a step between the upper step and the lower step, and for example in a step located halfway up the coil.
Les particules solides circuleront ainsi sur la bande de la spire ou bande de circulation du pas, cette bande de circulation étant délimitées par les bords internes et externes de chaque pas.The solid particles will thus circulate on the band of the turn or circulation band of the step, this circulation band being delimited by the internal and external edges of each step.
C'est le règlage du système de vibration, dépendant essentiellement de la taille des particules à séparer et de leur quantité, c'est-à-dire de leur vitesse d'introduction dans la spire, qui permet la séparation désirée. On aperçoit au voisinage du pas d'introduction des solides, une circulation assez confuse des mélanges de billes et ou des brisures avec notamment une amorce de descente de toutes les particules, les plus petites étant entraînées par les plus grosses, mais de façon inattendue ensuite, les billes les plus petites ou les brisures se mettent à circuler de bas en haut, en majeure partie entre le long des bords internes de la bande de circulation de chaque pas et la partie médiane de la surface de circulation délimitée par la surface du pas, et remontent à contrecourant des billes les plus larges. Quant aux billes les plus larges, elles descendent le long de la spire, avec une vitesse qui s'accélère de sorte que sous l'effet de la force centrifuge, les grosses billes roulent de plus en plus à la périphérie de la spire, c'est-à-dire en majeure partie entre les bords externes de la bande de circulation de chaque pas et ladite partie médiane du pas. De ce fait, progressivement et sans se gêner, les billes descendent le long des bords extérieurs des pas de la spire à contrecourant des petites billes ou des brisures qui cheminent de bas en haut, le long des bords internes des pas de la spire.It is the adjustment of the vibration system, essentially depending on the size of the particles to be separated and their quantity, that is to say their speed of introduction into the coil, which allows the desired separation. We see in the vicinity of the pitch of introduction of the solids, a rather confused circulation of the mixtures of balls and or broken pieces with in particular a primer of descent of all the particles, the smallest being entrained by the largest, but unexpectedly then , the smallest balls or the broken pieces start to circulate from bottom to top, mainly between along the internal edges of the circulation band of each step and the middle part of the circulation surface delimited by the surface of the step , and go up against the widest logs. As for the larger balls, they descend along the whorl, with a speed which accelerates so that under the effect of centrifugal force, the large balls roll more and more on the periphery of the whorl, c that is to say mainly between the outer edges of the circulation band of each step and said middle part of the step. Therefore, gradually and without hindering, the balls descend along the outer edges of the steps of the turn against small beads or broken pieces that travel from bottom to top, along the inner edges of the steps of the turn.
Le système de vibration est soumis à un règlage approprié fonction de la nature et des dimensions des particules à soutirer.The vibration system is subject to an appropriate adjustment depending on the nature and dimensions of the particles to be withdrawn.
Sur la figure 1, les petites billes ou les brisures sont évacuées en haut par la conduite 3, les billes de la taille désirées étant récupérées par la conduite 2 au bas de la spire.In FIG. 1, the small balls or the broken pieces are evacuated at the top by the pipe 3, the balls of the desired size being recovered by the
La figure 2 représente l'appareil de la figure 1, vu par dessus.Figure 2 shows the apparatus of Figure 1, seen from above.
On a procédé à des essais de séparation de mélanges de particules solides :
- le mélange envoyé par la conduite 1 de la figure 1 comportait 3 types de particules :
- - billes d'environ 2,54cm de diamètre (1 inch), chaque bille pesant environ 21,3g.
- - billes d'environ 1,27cm de diamètre (1/2 inch), chaque bille pesant environ 5,2g.
- - brisures pesant chacune, selon les tailles, 0,5 à 15g.
- the mixture sent via line 1 of FIG. 1 contained 3 types of particles:
- - beads about 2.54cm in diameter (1 inch), each ball weighing about 21.3g.
- - beads approximately 1.27cm in diameter (1/2 inch), each ball weighing approximately 5.2g.
- - broken pieces each weighing, depending on the size, 0.5 to 15g.
Chacun de ces 3 types de particules représente 1/3 en volume du mélange total.Each of these 3 types of particles represents 1/3 by volume of the total mixture.
On a utilisé une spire de 4,5 pas, la largeur du pas étant 10cm.We used a whorl of 4.5 steps, the width of the step being 10cm.
Dans un premier essai, on a réglé à 2mm l'amplitude des vibrations : on a observé que les brisures sont animées d'un mouvement de vibration tel que, par micro-projection successives sur le pas, elles s'élèvent dans la spire et sortent de la spire par le conduit 3 alors que les billes de diamètres 2,54cm et 1,27cm descendent vers le bas ou restent dans la partie inférieure de la spire, et finissent par s'évacuer par le conduit 2.In a first test, the amplitude of the vibrations was adjusted to 2mm: it was observed that the breaks are animated by a vibration movement such that, by successive micro-projection on the step, they rise in the coil and leave the coil via the conduit 3 while the balls of diameters 2.54cm and 1.27cm descend downwards or remain in the lower part of the coil, and end up being evacuated through the
Dans un deuxième essai, on a réglé à 3,5mm l'amplitude des vibrations : on a observé ici que les billes de diamètre 1,27cm s'élèvent également avec les brisures, et qu'ainsi, seules sortent par le conduit 1 les billes de 2,54cm de diamètre.In a second test, the amplitude of the vibrations was adjusted to 3.5 mm: it was observed here that the 1.27 cm diameter balls also rise with the breaks, and that thus, only come out through the conduit 1 2.54cm diameter beads.
D'autres essais effectués sur des mélanges de billes de diamètre 0,63cm (1/4 d'inch), 1,27cm (1/2 inch), 1,90 (3/4 d'inch), 2,54cm (1 inch) et 5,08cm (2 inch) ainsi que sur des brisures de ces différentes granulométries, montrent qu'en choisissant la bonne amplitude, on peut, dans tous les cas, séparer les matériaux sphériques ou ovoïdes des particules comportant une ou plusieurs surfaces planes et ceci avec des rendements allant de 95 à 98% dans les cas les plus défavorables et avec 99 à 100% d'efficacité dans la majorité des cas.Other tests carried out on mixtures of diameters 0.63cm (1/4 inch), 1.27cm (1/2 inch), 1.90 (3/4 inch), 2.54cm ( 1 inch) and 5.08cm (2 inch) as well as on the breaks of these different particle sizes, show that by choosing the right amplitude, one can, in all cases, separate the spherical or ovoid materials from the particles comprising one or more flat surfaces and this with yields ranging from 95 to 98% in the most unfavorable cases and with 99 to 100% efficiency in the majority of cases.
Claims (5)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8515947A FR2588783B1 (en) | 1985-10-23 | 1985-10-23 | METHOD AND APPARATUS FOR PERFORMING THE SEPARATION OF SPHERICAL MATERIALS WITH OR WITHOUT IMPERFECTIONS |
FR8515947 | 1985-10-23 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0223639A1 true EP0223639A1 (en) | 1987-05-27 |
EP0223639B1 EP0223639B1 (en) | 1990-09-12 |
Family
ID=9324243
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP86402142A Expired - Lifetime EP0223639B1 (en) | 1985-10-23 | 1986-10-01 | Method of and device for putting apart spherical materials possibly showing imperfections |
Country Status (6)
Country | Link |
---|---|
US (1) | US4986424A (en) |
EP (1) | EP0223639B1 (en) |
JP (1) | JP2620854B2 (en) |
CA (1) | CA1315738C (en) |
DE (1) | DE3674156D1 (en) |
FR (1) | FR2588783B1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4839031A (en) * | 1986-12-09 | 1989-06-13 | Europeenne De Retraitement De Catalyseurs Eurecat | Process for performing the separation of extruded materials which may or may not show imperfections |
US5082552A (en) * | 1986-03-10 | 1992-01-21 | Cri International, Inc. | Hydrotreating with catalyst particles using length and density grading |
CN106111544A (en) * | 2016-08-17 | 2016-11-16 | 南京西普水泥工程集团有限公司 | Ball mill grinding body sorting device |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8322538B2 (en) * | 2009-08-19 | 2012-12-04 | Janssen Bill M | Method and apparatus for separating fines from rock |
US20150020597A1 (en) * | 2013-07-17 | 2015-01-22 | Sanyasi R. Kalidindi | Accelerated powder segregation testing apparatus and method |
DE102017004272B3 (en) * | 2017-05-04 | 2018-06-28 | Doppstadt Familienholding Gmbh | Device for classifying classed goods |
CN108722870B (en) * | 2018-04-17 | 2021-01-15 | 张掖市农业科学研究院 | Screening machine and screening equipment |
CN111822363A (en) * | 2020-07-02 | 2020-10-27 | 江苏奥力斯特科技有限公司 | Spiral gravity screening method and device for pills |
CN114733768A (en) * | 2022-04-15 | 2022-07-12 | 国药集团中联药业有限公司 | Centrifugal pill selecting machine |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2724498A (en) * | 1954-11-18 | 1955-11-22 | David O Beresford | Device for separating mixed masses of spherical and irregularly shaped bodies such as seeds, grains and the like |
US2936072A (en) * | 1958-06-04 | 1960-05-10 | Gulf Research Development Co | Nutating helicoid separating apparatus |
US3464550A (en) * | 1967-05-04 | 1969-09-02 | Dow Chemical Co | Continuous solid particle shape classifier |
EP0075345A2 (en) * | 1981-09-23 | 1983-03-30 | Shell Internationale Researchmaatschappij B.V. | Apparatus and process for separating solids of different shapes |
GB2108871A (en) * | 1981-11-06 | 1983-05-25 | Shell Int Research | Apparatus for classifying catalyst particles and catalytic process employing catalyst particles thus classified |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1044067A (en) * | 1912-06-01 | 1912-11-12 | Charles L Mckesson | Method and apparatus for sizing or volumetric grading of materials. |
FR568010A (en) * | 1923-06-27 | 1924-03-13 | Helical sorter with adjustable spirals for seeds of all kinds | |
US2875895A (en) * | 1952-09-26 | 1959-03-03 | John B Traylor | Sizing machine |
US2778498A (en) * | 1954-07-02 | 1957-01-22 | Ici Ltd | Separation of materials |
US2974799A (en) * | 1958-07-08 | 1961-03-14 | Gulf Research Development Co | Oscillating helicoidal separating device |
US3085070A (en) * | 1960-04-22 | 1963-04-09 | Atlantic Refining Co | Method for separating solid oxides from ion exchange resins |
GB1297788A (en) * | 1969-08-25 | 1972-11-29 | ||
US3743093A (en) * | 1972-01-20 | 1973-07-03 | A Klancnik | Sorting machines |
US4022638A (en) * | 1975-08-05 | 1977-05-10 | Dart Industries Inc. | Continuous recovery of base metal from insulated wire scrap |
US4009783A (en) * | 1975-10-02 | 1977-03-01 | The United States Of America As Represented By The Secretary Of Agriculture | Friction separator |
US4070274A (en) * | 1976-03-11 | 1978-01-24 | United States Steel Corporation | Coarse concentrated iron ore for catalytic purposes |
US4295569A (en) * | 1979-09-25 | 1981-10-20 | The Terrell Machine Company | Apparatus for sorting textile bobbins |
US4583645A (en) * | 1982-12-02 | 1986-04-22 | Shoichi Yamamoto | Vibratory grain separating apparatus used with rice-hulling apparatus |
DE3301588A1 (en) * | 1983-01-19 | 1984-08-09 | W. Schlafhorst & Co, 4050 Mönchengladbach | SPOOL SEALING DEVICE |
-
1985
- 1985-10-23 FR FR8515947A patent/FR2588783B1/en not_active Expired
-
1986
- 1986-10-01 EP EP86402142A patent/EP0223639B1/en not_active Expired - Lifetime
- 1986-10-01 DE DE8686402142T patent/DE3674156D1/en not_active Expired - Fee Related
- 1986-10-23 CA CA000521256A patent/CA1315738C/en not_active Expired - Fee Related
- 1986-10-23 JP JP61253514A patent/JP2620854B2/en not_active Expired - Lifetime
-
1990
- 1990-02-20 US US07/481,687 patent/US4986424A/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2724498A (en) * | 1954-11-18 | 1955-11-22 | David O Beresford | Device for separating mixed masses of spherical and irregularly shaped bodies such as seeds, grains and the like |
US2936072A (en) * | 1958-06-04 | 1960-05-10 | Gulf Research Development Co | Nutating helicoid separating apparatus |
US3464550A (en) * | 1967-05-04 | 1969-09-02 | Dow Chemical Co | Continuous solid particle shape classifier |
EP0075345A2 (en) * | 1981-09-23 | 1983-03-30 | Shell Internationale Researchmaatschappij B.V. | Apparatus and process for separating solids of different shapes |
GB2108871A (en) * | 1981-11-06 | 1983-05-25 | Shell Int Research | Apparatus for classifying catalyst particles and catalytic process employing catalyst particles thus classified |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5082552A (en) * | 1986-03-10 | 1992-01-21 | Cri International, Inc. | Hydrotreating with catalyst particles using length and density grading |
US4839031A (en) * | 1986-12-09 | 1989-06-13 | Europeenne De Retraitement De Catalyseurs Eurecat | Process for performing the separation of extruded materials which may or may not show imperfections |
EP0274924B1 (en) * | 1986-12-09 | 1990-06-06 | EUROPEENNE DE RETRAITEMENT DE CATALYSEURS (en abrégé EURECAT) | Method for separating extruded materials with or without defects |
CN106111544A (en) * | 2016-08-17 | 2016-11-16 | 南京西普水泥工程集团有限公司 | Ball mill grinding body sorting device |
CN106111544B (en) * | 2016-08-17 | 2018-01-05 | 南京西普水泥工程集团有限公司 | Ball mill grinding body sorting device |
Also Published As
Publication number | Publication date |
---|---|
FR2588783A1 (en) | 1987-04-24 |
DE3674156D1 (en) | 1990-10-18 |
FR2588783B1 (en) | 1988-01-15 |
JP2620854B2 (en) | 1997-06-18 |
JPS62168583A (en) | 1987-07-24 |
EP0223639B1 (en) | 1990-09-12 |
CA1315738C (en) | 1993-04-06 |
US4986424A (en) | 1991-01-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1315738C (en) | Process and apparatus for the separation of spherical materials presenting and not presenting imperfections | |
EP0769462B1 (en) | Method and device to distribute uniformly a solid in a finely divided form in a vessel | |
EP0470142B1 (en) | Equipment for filling a container with a divided solid product | |
EP0345158B1 (en) | Apparatus for dust evacuation in bulk-discharging devices | |
JPH0271860A (en) | Centrifugal separation apparatus | |
BE1020736A3 (en) | PROCESS FOR THE GRANULOMETRIC SEPARATION OF MATERIAL RICH IN FILIFORM PARTICLES | |
CA1315739C (en) | Separation process for perfect or imperfect extruded materials | |
US4457746A (en) | Apparatus for centrifugal separation | |
JPS58500196A (en) | Separation device for particles from slurry | |
FR2614221A1 (en) | CENTRIFUGAL FORCE CLASSIFIER FOR SEPARATING A FINELY DISPERSED MATERIAL. | |
EP1931476B1 (en) | Method and device for concentrating substances in solid particle state | |
US607368A (en) | Machine for grinding and polishing | |
CA2107788A1 (en) | Tappered break roll | |
US3367499A (en) | Shaking-funnel device for the gravity concentration of solid particles | |
CH629158A5 (en) | PROTECTION DEVICE FOR APPARATUS FOR LOADING POWDERY OR GRANULAR MATERIALS. | |
EP1351761B1 (en) | Method for loading a chamber with solid particles | |
SU899125A1 (en) | Centrifugal classifier | |
FR2602438A1 (en) | AIR CLASSIFIER OF PULVERULENT MATERIALS | |
US3799343A (en) | Centrifuge and method | |
RU2094111C1 (en) | Device for producing granules | |
US2446717A (en) | Method and means for destroying froth | |
EP0085458B1 (en) | Sieving device | |
SU940879A1 (en) | Grain separator | |
RU2232650C2 (en) | Method of sorting-out loose materials | |
FR2523873A1 (en) | SEPARATOR INERTIA |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): BE DE GB IT LU NL |
|
17P | Request for examination filed |
Effective date: 19870624 |
|
17Q | First examination report despatched |
Effective date: 19880725 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: EUROPEENNE DE RETRAITEMENT DE CATALYSEURS (EN ABRE |
|
ITF | It: translation for a ep patent filed | ||
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE DE GB IT LU NL |
|
REF | Corresponds to: |
Ref document number: 3674156 Country of ref document: DE Date of ref document: 19901018 |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
ITTA | It: last paid annual fee | ||
EPTA | Lu: last paid annual fee | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19990921 Year of fee payment: 14 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19991022 Year of fee payment: 14 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19991029 Year of fee payment: 14 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19991116 Year of fee payment: 14 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20001001 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20001031 |
|
BERE | Be: lapsed |
Owner name: EUROPEENNE DE RETRAITEMENT DE CATALYSEURS EURECAT Effective date: 20001031 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20010501 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20001001 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20010501 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20010801 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 20011026 Year of fee payment: 16 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20021001 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20051001 |