• 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:
    Prior centrifugal concentrators for concentrating precious minerals use annular ribs or baffles to trap the precious minerals. Sand or magnetite tends to pack against such ribs, reducing the effectiveness of these devices. In the present invention, the inner surface of the rotating drum (2) is free of obstacles, but forms three continuous zones, a migration zone (A), a retention zone (B) and a lip zone (C). The precious mineral is retained in the retention zone by centrifugal force and friction while the unwanted slurry flows over the retention zone and out of the drum (2).
    公开号:SU1676440A3
    申请号:SU884355094
    申请日:1988-01-12
    公开日:1991-09-07
    发明作者:А.Мак Алистер Стивен
    申请人:Стивен А.Мак Алистер "Канада" (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to concentrators for the separation of particles of different specific gravities, and more specifically to centrifugal concentrators for the enrichment of gold ore.
    The purpose of the invention is to increase the efficiency of mineral separation.
    Ya figure 1 shows a hub with a partially cut-out outer chamber and with a fifth drum cover, general figure 2 - section A-A in figure 1; FIG. H - the same installation unit impeller; figure 4 - part of the wall of the hub section; Fig. 5 is a schematic representation of the forces acting on the frequency in the zone of movement.
    The concentrator includes a vertically located hollow drum 1 with an open end 2 and an inner surface 3, a device for supporting the drum 1 on an axis rotatably, and a drive 4 for rotating the drum 1 about an axis. A device for supporting the drum 1 on an axis rotatably includes
    five
    five
    a hollow shaft 5, lower bearings 6 mounted thereon and a bearing 7 mounted above the drum 1 for fastening the drum 1 rotatably around the feed pipe 8. The drive 4 is connected to the hollow shaft 5 by means of a belt drive consisting of pulleys 9 and 10 and the belt 11. The pulley 10 is fixed on the hollow shaft 5. The device for feeding the granular material includes a feed pipe 8 and a sludge supply line 12 connected to it and a water supply line 13. A cylindrical outlet chamber 14 is arranged coaxially around the drum 1. It includes an outer wall 15 and an inner wall 16. A drum 17 is located above the drum 1 and attached to it by means of nuts and bolts 18. In the lid 17 there are observation windows 19. The lid 17 is equipped with reinforcing ribs 20 With an outlet chamber 14, an outlet port 21 is coupled. In the lower part of the drum 1, an impeller 22 is installed, fitted with blades in its upper part.
    0
    five
    16 Polo is fixed above the bore shaft 5 by means of the support-1 of the same 23 and threaded rod 24, which connects with the possibility of separation the impeller 22 with axis 25 with the help of nuts 26.
    Holes 27 are provided in the holder 25 for passing a heavy fraction to the concentrate receiver 28. The impeller can be removed by removing one of the nuts 26 from the rod 24.
    The upper edge of the drum may have a protruding threshold 29 hanging over the inner wall 16 of the discharge chamber 14. The hollow shaft 5 also serves to drain the concentrate drum, for which a receiver 28 is provided. The inner surface 3 of the drum 1 is made from opposite zones of the drum 1 the displacement zone and the drain threshold and the retention zone located between them parallel to the axis of rotation, the displacement zone and the drain threshold zone being made expanding towards the containment zone. The inner surface 3 of the drum 1 is made of a displacement zone A which is outwardly directed, located above the displacement zone parallel to the axis of rotation of the holding zone B and above the retention zone inclined inward direction of the drain zone C. At the same time, the lengths of the zones of movement A, the hold B and the drain threshold C and the magnitude of the inclination of the zones of movement and the drain threshold are selected so as to create a component that has a sufficient force on the granular material to push the lighter granular material out of the drum 1 and granular material in the containment zone. In Fig. 2, zones A, B and C are indicated in the presence of material in the drum 1. The inner surface of the drum 1 is made free from obstructions to the flow of granular material. The axis of rotation of the drum may be located vertically. However, another arrangement of the axis of rotation of the drum 1 is also possible. The preferred inclination of the zones of movement A and the discharge stream C to the axis of rotation is 10: 1. In this case, the ratio of the lengths of the movement zone, the holding zone and the drain threshold zone is 6: 3: 1
    76440

    ten
    15
    20
    25
    Hub works log with lsd at kip im image.
    The drum 1 is rotated at a speed of speed in the direction of building K and in the lower hour continuously pp. Chrbana 1 is fed through the feed pipe 8 gold-containing pulp of the required conn
    At the outlet end, the feed pipe 8 may have a flow swirl nozzle for guiding the incoming pulp tangentially in the direction of rotation of the drum so as to add momentum to the pulp and thereby reduce the amount of power required to rotate the drum. The feed pipe 8 can also be fed through two separate feed lines — a sludge feed line 12 and a water feed line 13, whereby the relative content of water and sludge fed to the drum can be adjusted. The impeller 22 is provided with blades in its upper part and promotes pulp rotation,
    The flow of gold-containing pulp (Fig. 4), the exit from the pipe 8, twists and moves to the wall of the rotating drum 1. During the rotation of the pulp, the centrifugal force depending on the particle mass, the speed of rotation of the drum and the radius on which the particle is from the axis of the drum acts per particle and causes delamination of the pulp in such a way that the particles having the largest specific gravity are in the outer layer. The zone in which the layer of material of the highest specific gravity is located is indicated by the position a. The inner surface of the pulp is indicated by the position b. The pulp is usually divided into a layer of solid particles and an internal layer of water (due to the low specific weight of water), the boundary between which is indicated by the position c.
    In the first few seconds of operation, due to centrifugal force and the shape of the drum 2, a layer of particles accumulates in region d
    After this layer is deposited on the surface of the e portion, only particles with a large specific gravity remain. In the end, only the particles of the largest specific gravity, such as gold,
    thirty
    35
    40
    50
    55
    are held in zone B,
    its specific gravity
    ne These particles move to
    the particles below the pulp-top edge of the drum 1 are discharged into the outlet chamber 14 and removed through the outlet 21 from the concentrator. Materials of the highest specific gravity, such as gold, remain in the containment zone. When a sufficient amount of gold accumulates in the holding zone (approximately 1 pound in the case of a small drum), the rotation of the drum 1 is stopped and the drum is rinsed with water, washing out the concentrate through the hollow shaft 5 into the receiver 28 for the concentrate. In this case, the concentrate is removed through the passages between the disputable legs of the impeller 22 after stopping the rotation of the drum. When the drum rotates, the centrifugal forces prevent the material from leaving the drum through these passages. To facilitate the discharge of accumulated concentrate from the drum in the device, the method of unloading by means of water jets can be applied. Around the feed tube 8 in the rotor can be installed. Several spray nozzles, the outlet openings of which are directed to the holding zone in the drum.
    An effective device consists of four spray nozzles with a vertical flat spray tip, evenly distributed around the feed tube with the outlets tangentially directed from the feed tube towards the retention area in the drum. The spray nozzles are connected to a water source controlled by a valve. When a sufficient amount of concentrate is accumulated in the holding zone, the power is cut off through the supply pipe, the energy from the drum is turned off, the drum is allowed to rotate by inertia for a certain period of time, water is supplied from the source to the spray nozzles and the concentrate is washed out into the receiver 28, after which they again begin to rotate the drum and supply power through the feed pipe 8. The drum is allowed to rotate by inertia after turning off the power before opening the valve, which provides water for the spraying to the nozzles, usually for about 30
    The centrifugal force R (Fig.5) is valid
    imposes on particle P in the radial direction. The component of the centrifugal force acting along the surface 3 and denoted by the letter S is equal to
     . Q 20 25
    thirty . Q.,
    35
    50
    five
    the magnitude of the centrifugal force R, multiplied by the cosine of the angle about between the surface 3 of the displacement zone and the horizontal. The normal component of the centrifugal force is counteracted by the reaction N of the solid surface 3 of the displacement zone A. In the downward direction, a force G of gravity acts, which has a component directed along the surface of the zone of movement. The particle also acts in the direction opposite to the direction of movement of the particle, the friction force F, depending on the normal force N acting on the surface and on the particle friction coefficient and the surface. The rotational speed of the drum is chosen high enough, as a result of which the centrifugal force acting in the upward direction along the surface of the zone of movement is large enough for the resultant forces applied to the particle to act in the direction ijeepx along the surface of the zone of movement from
    For heavier gold particles to come into the outer layer of the pulp at a time appropriate for the particles to remain in the containment zone, the particle should spend a sufficient period of time in the transfer zone. Ideally, the transfer time should be long enough for the gold particle to , having started its movement upward along the zone of movement from the inner boundary to the pulp, moved to the layer closest to the wall of the drum and at the moment it reaches the holding zone. This moment thus depends on the quantity and consistency of the pulp. The speed of movement of the particles also depends on the specific gravity, particle size and shape of the precious mineral and other particles in the pulp and on the diameter and incline of the drum. The time of a given particle in the zone of movement also depends on the length of the zone of movement. Thus, the dimensions and slope of drum 1 depend on the type of pulp being processed and the speed at which it will be processed. In accordance with another option, the consistency and feed rate of the pulp can be adjusted to adapt the drum with the desired characteristics.
    The holding zone B consists of three subbands B, B. and B. The subzone B is a vertical annular portion of the drum wall. In the first moments of work, the deposition of particles of small specific gravity in this zone occurs and the surface friction here increases. The holding zone also includes a part B inclined in the outward direction of the movement zone and a part B inclined in the direction inward of the zone of the overflow threshold. When a particle passes into zone B, since the surface of this zone is vertical, the upward component of the centrifugal force disappears and when the particle enters the zone, it is transformed into a downward component. Increased surface friction also prevents movement. There is an upward component of force due to friction with particles moving upward in the outer layer, but it is ideally balanced by surface friction in the zone.
    Thus, particles of a heavier mineral accumulate in the containment zone until such time as the tidal force of the pulp flow overcomes the system of friction forces in the holding area and the downward component of the centrifugal force acting on the particle when it moves towards the inside. drain threshold. As soon as the precious mineral particles start to leave the holding zone, the Brabant stops and the concentrate is washed out to the receiver.
    The number of variables in the system can be changed with the corresponding changes in one or more other variables.
    When determining the optimal drum geometry, a large number of variables must be taken into account, but various theoretical approximations can be made to obtain the most appropriate range of slopes for the displacement zone to provide the required gold retention. For optimal motion characteristics, the tangent of angle 06, which is the angle between the plane, perpendicular to the axis of rotation, and the surface of the zone of movement, must be larger or larger.
    vein -7 l- / gt and less fi equals ft w
    .L
    Nf (pTrfV where
    - specific vertex particles, p Ј. —the specific gravity of water, N — the proportion of solid particles in the pulp, and f — the coefficient of kinetic friction of the wall surface at the corresponding velocity. This expression is used when solid particles are only submerged.
    Example. In the experimental device, the drum had the following dimensions: the length of the displacement zone is 12 inches (30, 48 cm); slope of the movement zone 10: 1 (vertical-horizontal); retention zone length 6 inches (15, 24 cm); drain zone length 2 inches (5 cm); the slope of the drain threshold zone is 10: 1 (vertical - horizontal); diameter in the middle of the zone of movement 8.8 inches (22.3 cm); diameter in holding area 10 inches (25.4 cm); the diameter of the upper edge of the zone of the drain PG horn 9.4 inches (23.9 cm).
    The pulp to be processed contained approximately 70% water (by weight), 28% sand and 2% magnetite and was fed at a speed of 5 t / h and at a speed of 13 t / 4 A small amount of gold was added to check the effectiveness of the device. It was found that in the case when the gold particles had a size of less than 1 mm, 90% of gold was extracted with a productivity of 5 tons / h and 50-70% with a productivity of 13 tons / h. When the gold particles had dimensions in the range of 1-2 mm, 95% of gold was extracted with lower productivity and 85-95% with higher productivity.
    Similar tests were also carried out using larger gold particles with a capacity varying from 7 to 13 tons / hour, and all gold particles were recovered.
    权利要求:
    Claims (6)
    [1]
    1. A concentrator for separating a higher specific gravity granular material from a lower specific gravity material, including a hollow drum with an open end, a device for supporting the drum on an axis rotatably, a device for feeding the granular material and a drive for rotating the drum around an axis, different the fact that, in order to increase the efficiency of the material separation process, the inner surface of the drum is made of zones located at the opposite ends of the drum Neither the drain threshold area and the retention area located between them parallel to the axis of rotation, the movement area and the drain threshold area expanding towards the holding area, and the lengths of the movement areas of the holding and drain threshold and the slope of the movement areas and drain threshold made with the possibility of creating a force acting on the granular material, which is sufficient to push the lighter granular material out of the drum and hold a heavier hard-bodied material la in retention zone. .
    0
    [2]
    2. A concentrator according to claim 1, characterized in that the inner surface of the drum is made free from obstacles to the flow of granular material.
    [3]
    3. Concentrator according to, characterized in that the axis of rotation is located vertically.
    [4]
    4. The concentrator according to claim 1, about tl and is due to the fact that the slope of the zone of movement to the axis of rotation is 10: 1.
    [5]
    5. The concentrator according to claims 1 and 4, which is the fact that the slope of the zone of the drain threshold to the axis of rotation is 10: 1.
    [6]
    6. Concentrator on PP. 1.4 and 5, characterized in that the ratio of the length of the zones of movement, retention and discharge threshold is 6: 3: 1.
    ten
    Aa
    I
    25 27
    W
    Fig.Z
    FIG L
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    同族专利:
    公开号 | 公开日
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    引用文献:
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    AU563414B2|1982-12-06|1987-07-09|Broken Hill Proprietary Company Limited, The|Centrifugal separation method and apparatus|FR2671985B1|1991-01-30|1993-04-09|Snecma|CENTRIFUGAL OIL FILTER WITH PARTICLE COLLECTION.|
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    US5222933A|1992-03-20|1993-06-29|Benjamin V. Knelson|Centrifual discharge of concentrate|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US07/002,805|US4824431A|1987-01-13|1987-01-13|Centrifugal concentrator|
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