Abstract: The invention relates to a method for increasing the concentration of platinum group metals in urban waste material. The method comprises obtaining particles of urban waste material; screening the particles of urban waste material by size,—selecting particles of urban waste material that lie within a defined size range; and processing the selected particles using at least one physical or chemical technique whereby to increase the concentration of platinum group metals to at least 5 ppm. The invention also relates to an apparatus for increasing the concentration of platinum group metals in particulate urban waste material. The apparatus comprises: a drying unit (4), a particle size screening unit (5); and one or more processing units for effecting platinum group metal concentration of the particulate urban waste material by physical and/or chemical techniques, in particular a magnetic separation unit (7) and a froth flotation cell (9).

Abstract: It is an object of the present invention to provide a screen apparatus having a function of dilute water which is suitable for a centripetal type screen which rotates inside the screen. A screen apparatus A comprises a tank 1 for receiving paper raw materials including an entrance 1c for the paper raw materials, a selection exit 1d and a foreign matter exit 1e, a cylindrical screen 2 fixed in the tank 1 and dividing the tank 1 into a primary chamber 1a and a secondary chamber 1b, and a stirring member 3 which is rotatably supported inside the screen 2 for stirring the paper raw materials.

Abstract: A separator (1) for separating dense particulates from slurry includes a sealed housing (2) enclosing a submerged screen bed (33) which allows dense particulates to fall into a hutch (6) from which they may be discharged. The housing has a slurry inlet (4) arranged to deliver slurry to a sump (3) which directs slurry to flow radially over the bed. An annular cavity (23) formed between the housing and bed receives tailings flowing off of the top of the bed. An outlet (7) from the annular cavity allows discharge of the tailings, and a liquid inlet (30) to the hutch provides an upward flow of liquid through the bed. The bed is agitated to assist passage of dense particulates.

Abstract: Separating elements (14) arranged about a central shaft (1a) rotate in common about the main axis (A) and individually about their longitudinal axes (B). A centrifugal distributor (6) distributes fine-grain mineral mixture mixed with fluid uniformly to the separating elements (14). In each separating element (14) the partial material flow (2a) is set in rotation about the longitudinal axis (B) by entrainment vanes (18) arranged in a first separating element section (15a) and the heavy fraction is centrifuged on to the separator wall (16a). In the second section (15b), formed as conical tubular worm conveyor, which contains no entrainment vanes, the heavy fraction is transported to the collecting chamber (21) and discharged through first discharge openings (22), the fine-grain mineral mixture being fluidized in pulsation on the separating wall (16b) by the combined rotating movements and the heavy fraction being concentrated.

Abstract: A centrifugal jig to beneficiate ore by separating a heavier particulate fraction from a lighter particulate pulp. The jig provides a rotor with a vertical cylindrical jig screen rotating in a fluid filled hutch to support a vertical jigging bed. The jigging bed is pulsed sequentially as it is rotated past plural spaced pulsing elements positioned in the hutch externally of the jigging screen. Pulsing may be by pressurized air in the form of fine bubbles, by pressurized fluid or a combination of both. Pulp material is fed at the bottom of the jigging screen to move upwardly thereacross with the lighter gangue material exiting above the screen for exhaustion and the heavier mineral bearing fraction exiting through the screen for subsequent recovery from the bottom periphery of the hutch area. The jig may be used as a bedded centrifuge or in the fashion of a traditional jig especially as when provided with ragging.

Abstract: A solids separator (10) is provided for separating solid particulates according to the density of individual particles. The separator (10) includes a cylindrical container (12) having a container bottom (22) carrying a drive shaft member (28). A cylindrical perforated liner (62) is releasably mounted concentrically within the container (12) on an elevated plate member (70) with an annular liquid jacket (80) being defined by the interior surface of the container and the exterior of the liner. An opening into the top of the container is used to introduce solids into the liner. Provision is made for injecting a liquid under pressure into the container which comprising a liquid source connected with a liquid conduit (46) received in a coaxial passageway (30) in the drive shaft member. A vacuum source, including a vacuum tube (82) mounted independently of the container and extending into the liner, is provided to extract the solid particulates of a specific density from preselected locations within the container.