Systems and methods for separating materials and recovery of valuable materials such as from end-of-life vehicles and appliances are disclosed. Vehicles are shredded and resulting pieces are dropped into a fluidic separator that separates the shredded vehicle scrap into heavier pieces and lighter pieces. The fluidic separator separates the bulk of the more valuable metals of the non-metals. The fluidic separator, which may be used for separating many kinds of mixtures of pieces of varying specific gravity, comprises a fluid-filled container in which the pieces and the fluid are stirred so that pieces of specific gravity greater than that of the fluid tend to sink and pieces of specific gravity less than that of the fluid tend to float.

Provided is a gravity separation device wherein occurrences of shelving, flashing, and the like inside the device can be suppressed, variations in the flow rate of underflow obtained by gravity separation can be minimized and underflow can be stably extracted. This gravity separation device, which separates overflow and underflow using differences in specific gravity from mixed material, is provided with a separation section that has a supply pipe for supplying a slurry of the mixed material at the top and separates that slurry into overflow and underflow, and a deposition section that is positioned below the separation section and wherein the underflow that has been separated by precipitation is deposited. An extraction pipe for extracting the underflow is connected to the deposition section, and a valve for extracting the underflow and a metering pump for quantitatively extracting the underflow are provided in the extraction pipe.

A cyclonic separation and materials processing method and system is presented in which materials entry at one end and which is arranged so that the materials that enter will be given a tangential velocity component as they enter. Specific embodiments include a three-dimensional sorting system with the use of an outward centrifugal motion and up/down (or vertical) motion flow of water or other media, which can be thought of as a three-dimensional separation.

A hydraulic particle separator is described. The particle separator comprises a main body having a top, a bottom, and a wall enclosing an interior cavity. At least one feed port is disposed on the top of the main body to introduce crude particle mixtures. A partition disposed within the cavity separates the cavity into a lower chamber and an upper chamber. The partition has at least one orifice for fluidic communication between the upper chamber and lower chamber. One or more grooves extend vertically along the interior surface of the wall. At least one tangential flow inlet port is disposed along the wall of the upper chamber above the partition.

A method of recycling a filler included in artificial turf by sorting the filler into two or more materials, including: a first sorting operation of sorting the two or more materials based on a grain size; and a second sorting operation of sorting the materials, which are sorted by the first sorting operation and have grain sizes belonging to a predetermined range, based on specific gravity.

Devices, systems, and methods for separating incinerator combined ash are described. The devices, systems, and methods include a fines process that utilizes water or other liquid in the separation of portions of the incinerator combined ash.

The disclosed Hydro-Gravitational Trap (HGT) method and apparatus separate a suspension into two flow streams, discriminating particles based on a designated particle settling velocity: one Designated Particle Concentrated (DPC) and one Designated Particle Diluted (DPD). The HGT confines particles between a controlled upward hydrodynamic field and the downward net gravitational field within the apparatus's High-Energy Segment (HES), awaiting removal. The HES typically contains an internal agitator conforming to its divergent shape. Agitator motion prevents trapped particles from adhering to the HES, provides flocculation energy, and mixes the contents, controlling the DPC flow stream concentration. The agitator can also simultaneously function as a control valve or an actuator regulating this flow in some preferred embodiments. Designated particles remain trapped in the HES until removed with the DPC flow stream while the DPD flow stream advects upward, exiting the apparatus through the top of the Low-Energy Segment (LES).

The present invention includes a mining system adapted to change underwater mining by selecting and harvesting only the target ore or gem. It eliminates costly displacement in mass of ore or material to the surface or shore, reduces pollution of the water column, and minimizes disturbance of the environment. The system includes a trommel fluidly coupled to separators, wherein each separator uses a vortex-like flow pattern to separate high-density sediment from lower density sediment based on flow rate. The present invention is the capable of separating and collecting various sized of desired ore in one pass. Additionally, the system is adapted to be coupled with a ROV dredge to reduce or eliminate diving time and risk of human life.

A separator device (100) includes a separation chamber (107) defined at its lower end by a fluidization fluid panel (111). The separation chamber (107) receives incoming slurry (113) via a slurry inlet (102). The separator device may be characterized in that means (122) for supplying pre-sheared aerated fluidization fluid is provided above the fluidization fluid panel (111). The means (122) for supplying pre-sheared aerated fluidization fluid includes a novel sparger (119) comprising a flexible perforated membrane which is configured to supplementally shear the pre-sheared aerated fluidization fluid and uniformly distribute microbubbles (129) throughout the separation chamber (107).

A hydraulic density separation device for separating a heavy material fraction with components of higher density from a light material fraction with components of lower density from a feed material includes a conveying device for conveying away the heavy material fraction, receiving chamber which can be filled with water for receiving the feed, a flow generator for generating a water flow in the receiving chamber and a water-fillable separation chamber for receiving the light material fraction. The conveying device has a shaft with a screw conveyor section for conveying the heavy material fraction out of the receiving chamber. The flow generator is designed and arranged such that a flow path of the water flow leads from the receiving chamber into the separation chamber. The conveying device has, in addition to the screw conveyor section, at least one washing section having a plurality of separate paddles arranged on the shaft.