• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Method of separation of a mixture of mineral grains with differentiated specific gravity, under the conditions of a restricted sedimentation, in a cylindrical device, consists therein that the mixture A of the mineral with water is radially supplied to a trough 2 formed around the upper edge of the wall 1 of the water box. The mineral circulating in the trough 2 is desludged and partially separated according to the weight of the grains, and then, under pulsating action of the water, is displaced in a ring-shaped working trough along spiral trajectories towards the conduit 17 and 19 taking out the light fraction D and towards the conduits with a flap 16 for discharge of the heavy fraction C. The pulsating motion of the water is effected by compressed air being cyclically fed to the ring-shaped air chamber 6 via the pulsation valves 14 from a ring-shaped tank 5 arranged around the water box. From the air chamber 6 additional air chambers 7 extend radially beneath the sieve deck 7.
    公开号:SU797554A3
    申请号:SU762384263
    申请日:1976-07-20
    公开日:1981-01-15
    发明作者:Ендо Антони；Яхна Вацлав；Шэнсны Адольф
    申请人:Цэнтральны Осьредэк Проектово-Кон-Струкцыйны Машын Гурничых "Комаг"；
    IPC主号:
    专利说明:

    (54) METHOD FOR DIVIDING A MINERAL MIXTURE BY DENSITY AND A DEVICE FOR ITS IMPROVEMENT.
    at the same time, the diaphragm is mounted on the pipeline that discharges the light fraction.
    Figure 1 shows the flow in a cylindrical machine; figure 2 - the flow in the car, the name of the form, b 1 low to quadrilateral in FIG. 3 - jigging machine, general view; figure 4 is a plan view; Figures 5 and 6 illustrate a large capacity jigging machine designed to enrich minerals requiring intense pulsation of water; Figure 7 shows a device with pulp and water flows.
    The flow of a mixture of minerals in an aqueous medium, separated by the proposed method (FIG. 1.2), is carried out as follows.
    The mixture of mineral and water is brought to the outer wall of the jigging machines with an initial velocity of Vp-, which ensures the mixture to circulate along the way. At least, near the upper edge of the outer wall of the water box. The circulating stream of the mixture in the slit sieve is slimeless, and the smallest grains with part of the water flow out of the jigging machine through the paths t, and the rest flow through the spiral paths ty, and t in the direction of the central axis, and the light fraction moves along the path t. , and on a put m-fc - t is yellow fraction. As a result of the circulation of the suspension along the path m 1ts.,. as well as the flow along the spiral paths t and t (j is obtained the road L 7V 1-o which is necessary for complete separation of the mixture.
    The device (Fig.3,4) contains a water box, the upper edge of the outer wall 1 of which has the shape of a chute 2, open towards the central axis 3; The chute has a slotted sieve 4 with slots parallel to the generator of the cylinder. An inlet nozzle 5 is introduced into the sieve groove 2, feeding the mixture of a row mineral with water, with an initial velocity ensuring that the mixture circulates in this groove. In the inner part of the chute 2, the filtrate is collected, which consists of suspended fine grains of miners in water. On the outer side of the wall 1 below the chute 2 there is a storage bin 6 for compressed air and a collection manifold b for decompressed air. From the bin b, compressed air passes through the inlet of the pulsation channel 8 into the air chamber 9, from which it goes out through the outlet of the pulsation channel 8 into the collecting manifold 7. After the operation, the air chamber 9 is arranged below the sieve groove 2 along the inside of the water box 1 its upper part protrudes above the screen 10, made in the form of
    An overturned truncated cone or pyramid, with a large base resting on the wall of the air chamber 9, and a smaller base on the body 11 of the heavy fraction collection. The heavy fraction collection is a section of the pipeline having a diaphragm of 12 below. Depending on the amount of the heavy fraction on the pit floor 10, near the central axis 3, the diaphragm 12 is lowered or raised.
    The light fraction leaves the jigging machine through pipelines 13 and 14, it is removed through pipeline 15, and the undersize grains go to pipeline 16, from where they drain into water-draining devices.
    A high capacity jigging machine (figure 5, b) V is designed to enrich the mixture of minerals,
    containing a significant amount
    heavy fraction. Sieve 4 in chute 2 is slightly higher than the bottom of the chute to limit its wear to grains with strong abrasive properties. For the same purpose, it is possible to change the direction of the inflow of the mixture into the depositing machine through the inlet nozzles 5. The annular air chamber 9 is divided into sections by vertical radial walls
    17. From each section of the annular chamber 9, below the sieve deck .10, three additional chambers 18 are removed, passing radially relative to the body 11 of the heavy fraction collector.
    A common mineral with water A (Fig. 7) is brought to the chute 2 by the inlet nozzles 5. The bottom water B is also fed into the jigging machine through an opening in the bottom. The slurry, to the circular in the chute 2, is slime-free on the sieve 4. The mineral-free sludge is then moved on the sieve floor 10 when pulsating water moves along spiral paths in the direction of the axis 3 of the jigging machine. The light fraction is drained from the jigging line through conduit 13 and 14, the heavy fraction is removed through the collector with diaphragm 12 via conduit 15, and the grates through conduit 16 to the drainage devices.
    权利要求:
    Claims (4)
    [1]
    1. A method of separating a mineral mixture according to density in conditions of constrained fall in a cylindrical jigging chamber with pneumatic pulsation of water, which distinguishes AO so that, in order to increase the efficiency of the process by increasing the accuracy of separation, the mineral mixture with water brings the external contact of the cylindrical housing and direct the pulsating flow of the mixture in a spiral to the central axis. ..
    [2]
    2. Device 1D) An implementation for carrying out the method according to Claim 1, comprising a cylindrical body equipped with a water bath, the walls of which consist of separate sections, air chambers open to the bottom, a sieve deck, a source feed nozzle and collections of separation products, characterized by that the device is equipped with a chute installed at the upper edge of the housing and having at least one tangential nozzle for supplying the initial power supply a slotted sieve and a pipeline for draining the filtrate, an annular storage tank for compressed air and an annular manifold for decompressed air.
    [3]
    3. A device according to claim 2, characterized in that the air chamber is divided into a series of sections by vertical radial walls, each section being associated with a separate pulsation valve and provided with an additional air chamber located below the sieve deck.
    [4]
    4. The device according to claim 2, about tl and which is so that the collector of the heavy fraction is equipped with a diaphragm in the form of a disk with a drive, while the diaphragm is mounted on a pipeline that discharges the light fraction. Sources of information taken into account in the examination 1. USSR author's certificate 195977, cl. B 03 B 5/10, 1961.
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    类似技术:
    公开号 | 公开日 | 专利标题
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    GB2162092A|1986-01-29|Cyclonic froth flotation cell
    US2364405A|1944-12-05|Method and apparatus for separating foreign matter from papermaking material
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    US2726765A|1955-12-13|Density separation-method and apparatus
    US3374885A|1968-03-26|Method and apparatus for beneficiating minerals
    SU1528333A3|1989-12-07|Device for pneumatic classification of materials
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    US2869728A|1959-01-20|Apparatus for separating solid particles suspended in a liquid
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    SU599849A1|1978-03-30|Froth separation machine
    US1081267A|1913-12-09|Centrifugal concentrator.
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    WO1998025705A1|1998-06-18|Centrifugal separator with injection of fluidizing liquid between non-fluidized recesses
    SU1209304A1|1986-02-07|Multiple-stage hydraulic cyclone
    同族专利:
    公开号 | 公开日
    BR7604967A|1977-08-09|
    DE2630639A1|1977-02-03|
    CA1069859A|1980-01-15|
    AR209669A1|1977-05-13|
    IN145358B|1978-09-30|
    DE2630639B2|1978-02-02|
    GB1546714A|1979-05-31|
    DE2630639C3|1982-02-18|
    PL113266B1|1980-11-29|
    US4071440A|1978-01-31|
    FR2319424A1|1977-02-25|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3273714A|1966-09-20|Circular jigs |
    US128628A|1872-07-02|Improvement in ore-concentrators |
    US2134154A|1931-07-27|1938-10-25|Gen Mining & Finance Corp|Ore dressing jig|
    US2199091A|1938-12-03|1940-04-30|Anthracite Separator Co|Method and apparatus for separating solids of different gravities|
    US2287748A|1941-02-25|1942-06-23|Anthracite Separator Co|Apparatus for separating solids of different gravities|
    GB1153722A|1965-06-08|1969-05-29|Nat Res Dev|Improvements in or relating to the Gravity Separation of Granular Materials|
    US3519130A|1966-09-21|1970-07-07|Waclaw Jachna|Apparatus for classifying of finegrained solids in wet condition|
    GB1391256A|1971-04-20|1975-04-16|Birtley Eng Ltd|Apparatus for separating and classifying mixtures of particulate materials|
    US3773176A|1972-03-27|1973-11-20|J Loughner|Separating apparatus and method|US4231861A|1979-03-26|1980-11-04|Parsons Manufacturing, Incorporated|Grain cleaning apparatus|
    AT381718B|1982-01-20|1986-11-25|Voest Alpine Ag|ROTATING GAP SCREEN FOR DRYING SOLIDS, e.g. BROWN COALS|
    AU573960B2|1985-01-25|1988-06-23|LowanPty Limited|Centrifugal jig|
    AR240262A1|1985-01-25|1990-03-30|Lowan Management Pty|CENTRIFUGAL HYDRAULIC SCREEN.|
    IN174814B|1988-07-01|1995-03-18|Lowan Man Pty Ltd|
    EP0499769B1|1991-02-21|1997-07-02|Nzemba, Mukamba Kadiata|Gravimetric concentration process in a jig|
    MXJL00000004A|2000-06-23|2002-08-29|Escorza Simo I Castaneda|Sedimentation method and muds classification.|
    EP1767273A1|2005-09-27|2007-03-28|Genimin|Method and device for the concentration of solid particles|
    US7380670B2|2006-06-16|2008-06-03|Pelletron Corporation|Compact dedusting apparatus|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    PL1975182377A|PL113266B1|1975-07-28|1975-07-28|Method of separating the mixture of mineral particles contained in a watery medium and setting unit for separating the mixture of mineral particles|
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