APPARATUS FOR SIZING GRAINS BETWEEN 20 AND 300 MICRONS

Abstract: The housing (1) of the apparatus is of vertical arrangement and is divided by a partition wall (4) into a central (2) and an external part (3), so that sieve elements (5) form at least a certain part of it. The sieve elements (5) are arranged at an angle of up to 20<o> to the direction of the grain flow. Baffles (6) sloping outwards from the center of the housing (1) at an angle of 30-45<o> are arranged in the central part (2), while the external part (3) is provided with an overflow weir (14) and with an adjoining collecting channel (15) connected to the carrier circulating system. The common inlet of the material to be separated and the carrier medium as well as the outlet of the coarse grains (10) are connected to the central part (2) of the housing (1), while the outlet (16) of the fine grains is connected to the external part (3). The carrier medium circulating system may be closed or open and functions with gaseous or liquid medium. Accordingly, fan or pump and fine sludge- or dust separators are in the system. The sieve elements are replaceable and/or adjustable. The housing is preferably provided with flexible suspensions (19) and has a drive (17, 18) for improving the efficiency of the separation.

Description: APPARATUS POR SIZING GRAINS BETWEEN 20 A D 300 MICRONS Tlie invention relates to an apparatus for 5 sizing grains " between 20 and 300 microns comprising a housing, a sieve and a carrier medium circulating system. Materials /pigments, fillers and abrasives, etc/ containing grains of different sizes are frequently 10 required in the industry for separation into two phases, so that one phase contains mainly the grains smaller, and the other phase mainly the grains than a given grain size. Various sizers and/or dustse arators are known 15 for the separation of grains. Such are the cyclones, centrifuges, hydraulic classifiers and sieves, the use of which depends on the material to " be £ractioned, the sharpness of classification and the given techno¬ logy. a 20 Por the range of the 20 - 300 /U grain size, ge¬ nerally air-Jet sieve is used, if no excessively high pro cessing capacity is required. The main part of an air- j et sieve is a sieve drum revolving in a housing, along a slop ed shaft. The required fraction of the ma- 25 terial to " be sized is driven through " by a gaseous carrier medium " blown through the sieve drum in a radial direction, in ahout a quantity of 10-20 kp/h. The drawback of this apparatus is that most part of the surface of the ro tary sieve is covered " by the 30 . material to " be separated and hence - compared to the size of the apparatus - the active sieve surface is relatively small. The material sits on the sieve, the grains " blo ck up . the ap er-fcuresr and the sticking grains further deteriorate the efficiency. 55 On the other hand, due to the moving parts, the apparatus is sensitive to failure. The object of the invention is to provide an apparatus for the reliable sizing of grains between 20 and 300 U, with high output. 5 According to the invention, the housing of the apparatus is of vertical arrangement and is divided by a partition wall into a central and an external part, so that sieve element form at least a certain part of it. The sieve elements are arranged at an 10 angle of up to 20° to the direction of the grain flow. Baffles sloping outwards from the center of o the housing at an angle of 30-45 are arranged in the central part, while the external part is provid¬ ed with an overflow weir and with an adjoining -15 collecting -channel connected to the carrier medium circulating system. The common inlet of the material to be separated and the carrier ' -.medium as well as tne outlet- of the coarse ' grains are .connected to the central part of the house, while the outlet of the 20 fine grains is connected to the external part. The carrier medium circulating system may be clo sed or op en and func'tions with gaseous or liquid medium. Accordingly, fan or -pump and fine sludge- or dust separators are in the system. ^5 ■ ruie sieve elements are replaceable and/or ad¬ justable. The housing is preferably provided with flexible suspensions, and has .a drive for i prov i_g the ef¬ ficiency of the separation. The drive may be an ec- 50 centric disc connected mo tor. Similarly, the efficiency of separation can be improved if the carr ier medium circulating system is provided with a pulsator. In- the apparatus according to the invention, a 55 certain part of the coarse fraction can be separated 3 - by gravitation before the sieve surface and the other part mechanically on the sieve, The fine fraction flowing through the sieve surface, leaves through the outlet of the fine grains . 5 Arrangement of the sieve surface in a vertic¬ al or inward sloping position prevents the material from laying on the sieve, whereby the sieve surface remains clean, free from clogging, and functions with a output higher than the devices known in 0 the art. The main advantage of the apparatus is that contrary to the traditional apparatuses of 10-20 kp/h output, its output is 2-10 q/h /the output of the . known devices is 10-20 kp/n / and functions with high efficiency. With vibratory or wobbling mo tion, the effi¬ ciency of .the apparatus can be further improved, since flow of the medium on the sieve is constant¬ ly o varCa-oriente , which easily passes the grains - smaller than the apertur e through the sieve. How¬ ever, the grains slightly larger than the aperture, are inclined to get stuck in the aperture and they have to be removed continuously. Upon vibration, a certain part of tne grains falls out, but removal 5 of the more sticking grains necessitates to elimi¬ nate periodically the pressing-in effect of the medium-flow. This is accomplished by adjusting the motion as to .have the norizontal movement of the mesh panel faster than the velocity of the medium- o • -flow. There will always be a moment in each phase of the motion, when the sieve moves outwards faster than the medium-flow. Consequently, the grains can get detached f_?o__ the mesh panel. Tne separation can also be accomplished with pulsating medium-flow, but this is l ess efficient, and technically more complicated^ Further advantage of the apparatus is that it can be operated with gaseous as well as liquid carrier medium, and the sieves are replaceabl e according to the quality and the grain size of the material . Replacement of the sieves or a ustement of their po sition can be quickly and easily carried out. Since there is no ' moving part in the sizing space of the apparatus, its operation is reliable and the maintenance is fairly simpl e . Further details of the invention are describ ed by way of example with the aid of drawing, in which Figure 1 is a sectional view of the apparatus according to the invention, Figure 2 is the apparatus shown in Figure 1 , nctioning with a liquid carrier me ' dium, Figure 3 is the apparatus shown in Figure 1 functioning with a gaseous carrier medium . The apparatus shown in Figure 1 consists of a housing 1 divided by a partition wall 4 into a central part 2 and an external part 3. The - central part 2 of the partition wall 4 is formed by sieve elements 5, and baffles 6 are arrang ed in the central part 2 at the height of sieve elements 5. The baffl es 6 are sloping outwards from ' the centre¬ line of the internal space 2 to conduct the material to be s eparated on to the sieve elements 5. The angle of slope of "the baffles 6 is 30-45° . In the present example, the baffles 6 are truncated cone surfaces , having central openings 6a . The cro ss- section of the op enings is decreasing - downwards at each level . The lowest ba ffle may no t have any op ening at all . The half cone angle of the baffles /i . e . the angle of slo.p e/ is 40 to the vertical centreline . Of course, baffles of other forms may also be applied. They can have a form of a truncated pyramid or they can be simple plates as well . The sieve elements 5 may be similarly in a slightly tilted po sition, at an angle o f max. 20° to the vertical first of all, when no drive is provided. However, in the present embo diment the sieve elements 5 are vertical . Their distance from the end of the baffle s - 6 is. adjust- abl e . . The material charging hopper 7 is connected on the top to the central part 2 o f - the housing and the material to b e s eparated is admitted i_h ere troug into the apparatus . The carrier medium inlet stub 8 is also centrally lo cated, with the charging cone 9 underneath for setting the amount of material to be admitted. ■ The co ars e grain outlet stub 10 is connected to the internal space 2 and the fine grain outlet stub to the external space 3 of the house 1. Bo th stubs are provided with butterfly valves 12 and 13 and connected to a clo sed space, such as a container /with or without an elevator/ or a sluiced delivery. The housing 1 is provided on the top with an overflow weir 14 connected to a sloping collecting channel 15 , An outlet stub 16 is formed on its deepest point. In the course of op eration of the apparatus, the material to be separated passes into the a- terial charging hopp er 7, from where it is entrained by the carrier medium flowing thro ugh the inlet stub 8 in the quantity determined by the charging cone 9. Thus , the material passes into the central part 2 of the house 1 and to the baffles 6 , Frome there, it flows directly to the sieve elements 5, where the larger grains fall sown by gravitation between the baffle plates 6 and sieve elements 5. The further large grains hanging up on the sieve elements fall down' to the bo ttom of the central part 2 , from where they leave through the coarse grain outlet stub 10 . The fine fraction together with the carrier medium flows through the ap ertures of the sieve • elements 5 and leaves through the fine grain out¬ let s tub 11. The carrier medium- together viτh the finest fraction falls through the overflow weir 14 and from the coll ecting channel 15 it l eaves through the outlet s tub 16. Efficiency of the s eparation can b e improved by vibratory or wobbling mo tion o f the sieve. As mentioned earli er, the free si eve surface will be greater if the sieve mantle is in mo tion, since the grains become " shaken off the mantle. For this puspo se the housing 1 may be interconnected with an actuating mechanism. This is a mo tor 17 in the present embodiment, provided with an eccentric disc 18 through which it is connected to the housing 1. Movement of the housing 1 is enabled by flexible supports 19. As mentioned earlier, the apparatus according to the invention functions equally with liquid and gaseous carrier medium. A ' system functioning with liquid carrier medium is shown in Figure 2. As seen in the drawing, a closed carrier medium-circulating system 20 is connected to the outlet stub 16 of the collecting charm el 15. Here, the flow of the liquid is ensured by a pump 21 , For separation of the very fine fraction present in the discharged carrier medium, the carrier me¬ dium-circulating system 20 is provided with a fine sludge separator 22, From here the cleaned carrier medium returns to the carrier medium inlet stub 8. The fractions discharged from the apparatus are carried off by closed elevators 23 and 24. A version of the apparatus according to the invention functioning with gaseous carrier medium s shown in Figure 3. Eere, the carrier medium is not returned to the inlet stub .8, but after having been cleaned it is discharged into the surrounding air. This system is actuated by a fan 25 and the fine fraction in the medium is removed by cyclones 26 and 27. In view of the forego ing, it is evident that build-up of the apparatus according to the inven¬ tion is very simple, at the same time it carries out the separation of the media containing 20 to 300 microns grains extremely efficiently and reli¬ ably. There are no moving parts in the separating system, hence the wear is minimal, and the system does no t require maintenance. The sieves are replaceable and their position is adjustable. The apparatus functions equally with liquid and gaseous carrier medium, thus it can. be used in an extensive range. Naturally, the examples serve only for de¬ monstration of the apparatus .according to the invention, but obviously numerous other versions are also feasible within the scope claimed in the present application.

Claims: C L I M S 1. Apparatus for sizing grains between 20 and 300 microns, comprising a housing, sieve and a carrieϊ medium circulating system, c a a c ¬ t e r i z e d in that the housing /l/ is of ver¬ tical arrengement, divided by a partition wall /4/ into a central /2/ and an external part 3/, so that the sieve elements /5/ form at least a part of said partition wall /4/ and are arranged at an angle of up to 20° to the direction of the grain flow, a number of baffles /6/ are arranged in the central part /2/ of "the housing /I/, sloping out- wards from the center of the housing /I/ at an angle of 30--5°, the external ' part /3/ of the housing /l/ is provided with an overflow weir. 14/ and with a collecting channel /15/ connected to the carrier medium circulating system /2θ/., wherein the common inlet of the grains to be separated and the carrier medium a_ε well ' as the outlet 10/ of the coarse grains are connected to the central part /2/ of the housing /!/ while the outlet of the fine grains is connected to the external part /3/ of the housing A/. 2. The apparatus as claimed in claim 1, c h a ¬ r a c t e r i z e d in that the cross-section of the central opening of the baffle or between the baffles /6/ are decreasing on each level, 3. he apparatus as claimed in claim 1, c a ¬ r a c t e r i z e d in that the carrier medium circulating system /20/ is closed. 4. The apparatus as claimed in claim 1, c h a • r a c t e r i z e d in that the carrier medium circulating system /20/ is open. 5. The apparatus as claimed in claims 2 to 4 f c h a r a c t e r i z e d in that the carrier 5 medium circulating system /20/ is provided with a fan /21/ or pump /25/. 6. The apparatus as claimed in claims 1 to 5, c h a r a c t e r i z e d in that the carrier medium circulating system /2θ/ is provided with at 0 least one fine sludge- or dust separator /22,26,27/, 7. The apparatus as claimed in claims 1 to 6, c h a r a c t e r i z e d in that the sieve ele¬ ments /5/ are replaceable and/or adjustable. 8. The apparatus as claimed in claims -1 to 6, - 5 c h a r a c t e r i z e d in that the housing /!/ is of flexible suspension /19/ and. is provided with a drive. 9. The apparatus as claimed in claim 8, c h a ¬ r a c t e r i z e d in that the drive consists of J a motor /17/ and an excentric disc /18/. 10. The apparatus as claimed in claims 1 to 9, c h a r a c t e r i z e d in that the carrier medium circulating system /20/ is provided with a pulsator.

Inventors: CSILLAG ZSOLT, KALMAN TIBOR, LEGAT TIBOR, SOLYMAR KAROLY, SZENTGYOERGYI GEZA, ZSEMBERY LASZLO, CSILLAG, ZSOLT, KALMAN, TIBOR, LEGAT, TIBOR, SOLYMAR, KAROLY, SZENTGYOERGYI, GEZA, ZSEMBERY, LASZLO
Applicants: MAGYAR ALUMINIUM, MAGYAR ALUMINIUMIPARI TROESZT
Application year: 1986
Main classification: B07B7
IPC codes: B07B4, B07B7, B07B9