A process for separating Cesium and other elements from refuse. Crushed refuse is admixed with water from a water storage source. The admixture is transferred to a first cyclone separator to divide the admixture into a refuse rich slurry stream and a carbonaceous rich slurry stream. The refuse rich slurry stream is dewatered through a vibrating screen and the water collected sent to the raw feed sump source. The carbonaceous rich slurry is directed to a second cyclone separator to separate low quality carbon from high quality carbon, the high quality carbon is transferred to a third cyclone separator used to separate the element rich media water therefrom. The separated media water is returned via a siphon leg to the raw feed sump, and the dewatered high quality Cesium is available for markets.

A process for separating Cesium and other elements from refuse. Crushed refuse is admixed with water from a water storage source. The admixture is transferred to a first cyclone separator to divide the admixture into a refuse rich slurry stream and a carbonaceous rich slurry stream. The refuse rich slurry stream is dewatered through a vibrating screen and the water collected sent to the raw feed sump source. The carbonaceous rich slurry is directed to a second cyclone separator to separate low quality carbon from high quality carbon, the high quality carbon is transferred to a third cyclone separator used to separate the element rich media water therefrom. The separated media water is returned via a siphon leg to the raw feed sump, and the dewatered high quality Cesium is available for markets.

Systems and methods can sort materials of different specific gravities in a mixture. These systems and methods for separation of materials provide multiple forces simultaneously. The system can utilizes both vertical and the horizontal forces for efficient separation of materials with different specific gravities.

A process for separating a mixture of materials using a segregation media within a vessel having a central baffle structure which shuggles the mixture by oscillating the baffle structure at a frequency and amplitude. The mixture of materials may have overlapping densities with the segregation media having a density within the overlapping region. Polymers PE and PP may be separated in flake form. For a mixture of materials of differing densities, water may be the segregation media. Shuggling is combined with controlling the flow of water through the vessel at a set velocity. Embodiments are described for separating plastics and mineral ore.

A process for separating a mixture of materials using a segregation media within a vessel having a central baffle structure which shuggles the mixture by oscillating the baffle structure at a frequency and amplitude. The mixture of materials may have overlapping densities with the segregation media having a density within the overlapping region. Polymers PE and PP may be separated in flake form. For a mixture of materials of differing densities, water may be the segregation media. Shuggling is combined with controlling the flow of water through the vessel at a set velocity. Embodiments are described for separating plastics and mineral ore.

The present disclosure describes a method of separating particles using a combination of acoustophoresis and acoustic fluid relocation. The disclosure also describes a microfluidic device that can be used to separate particles using a combination of acoustophoresis and acoustic fluid relocation. The disclosure describes methods of separating nanoparticles, microparticles, nanoparticles from microparticles, and micron-sized particles from sub-micron-sized particles.

The present disclosure describes a method of separating particles using a combination of acoustophoresis and acoustic fluid relocation. The disclosure also describes a microfluidic device that can be used to separate particles using a combination of acoustophoresis and acoustic fluid relocation. The disclosure describes methods of separating nanoparticles, microparticles, nanoparticles from microparticles, and micron-sized particles from sub-micron-sized particles.

A cyclical and continuous device and method for wet sieving of polysaccharide granules are provided. The device includes a first dosing tank, a second dosing tank connected to the first dosing tank by a first circulation pump, a first suction filtration tank connected to the second dosing tank by a second circulation pump, and a second suction filtration tank connected to the first dosing tank by a third circulation pump. An overflow port provided on a side wall of the second dosing tank is higher than a feed port of the first dosing tank. A sieve of a mesh filter for coarse powder is disposed in the first dosing tank. A sieve of a mesh filter for fine powder is disposed in the second dosing tank. A stirring device is disposed in both the first dosing tank and the second dosing tank.

A cyclical and continuous device and method for wet sieving of polysaccharide granules are provided. The device includes a first dosing tank, a second dosing tank connected to the first dosing tank by a first circulation pump, a first suction filtration tank connected to the second dosing tank by a second circulation pump, and a second suction filtration tank connected to the first dosing tank by a third circulation pump. An overflow port provided on a side wall of the second dosing tank is higher than a feed port of the first dosing tank. A sieve of a mesh filter for coarse powder is disposed in the first dosing tank. A sieve of a mesh filter for fine powder is disposed in the second dosing tank. A stirring device is disposed in both the first dosing tank and the second dosing tank.

An apparatus for processing aggregate material comprising an inclined trough having a pair of shafts rotatably mounted therein, the shafts having staggered blades arranged pass between one another during rotation of the shafts and angled to carry material towards an upper end of the trough, excess water and any floating trash passing over a weir adjacent a lower end of the trough onto the deck of a first vibratory screen, and a second vibatory screen being mounted adjacent the upper end of the trough for receiving particulate material from the upper end of the trough, the second vibratory screen having at least one deck for grading the material, wherein water collected in a sump of the first vibratory screen is arranged to pass into a sump of the second vibratory screen.