Systems and methods for cryogenic separation of plant material are provided. A vessel is filled with cryogenic fluid having a temperature at or less than −150 degrees Celsius. Plant material is placed into the vessel via a basket and agitation is provided to the plant material in the vessel for a predetermined time period. Upon completion of the time period, the basket having at least a portion of the plant material is removed from the vessel. Plant particulates separated from the plant material during the agitation settle to the bottom of the vessel. The vessel is drained of the cryogenic fluid, including plant particulates separated from the plant material.

Systems and methods for cryogenic separation of plant material are provided. A method of cryogenic separation of plant material, includes placing a sieve into a vessel. Plant material is placed in the sieve. Cryogenic fluid is provided at or below −150 degrees Celsius to the sieve. The plant material is agitated within the sieve and the vessel to separate plant particulates solidified by the cryogenic fluid from the remainder of the plant material. The cryogenic fluid and plant particulates are removed from the vessel.

A system for separating materials from a waste stream includes multiple processing units arranged linearly, each configured to employ a density separation process. The system incorporates a paddlewheel or similar agitator in one or more of the units, thereby providing enhanced control over the agitation and forces used to separate heavier fractions from lighter fractions. By adjusting paddlewheel speed and other operational parameters, residence times in each unit can be optimized to maximize overall separation efficiency.

A system for separating materials from a waste stream includes multiple processing units arranged linearly, each configured to employ a density separation process. The system incorporates a paddlewheel or similar agitator in one or more of the units, thereby providing enhanced control over the agitation and forces used to separate heavier fractions from lighter fractions. By adjusting paddlewheel speed and other operational parameters, residence times in each unit can be optimized to maximize overall separation efficiency.

This application discloses a separator for separating and recovering materials from a waste stream. The separator has a cyclone having a top section and a bottom section, an impeller within the cyclone, a media inlet for accepting a flow of media or a pulsating flow of the media operatively connected to the impeller in which media or fluid flows through the impeller into the separator; a first discharge passage for a collecting a light fraction, and a second discharge passage for collecting a heavy fraction.

A system for separating coal from iron oxide and sulfur comprises a first tank having crusher to grind the coal. Steam is directed into the first tank to mix with the coal to produce a maximum substrate area for chemolithotrophic bacteria and algal species to act upon. A mechanical pulverizer is fed with the coal and steam. A sieve and a second tank receiving the coal from the pulverizer apparatus. An air exchanger connected to the second tank collects nanosized particulates of coal. A pipeline feeds the coal within the second tank with a mixture of chemolithophic bacteria from a breeding tank. A holding tank receives the mixture of coal and chemolithophic bacteria. A centrifuge receives the mixture of coal and chemolithophic bacteria from the holding tank and separates the coal from the mixture. A fourth tank receive the separated and hydrated coal particles from the centrifuge.

A system for separating coal from iron oxide and sulfur comprises a first tank having crusher to grind the coal. Steam is directed into the first tank to mix with the coal to produce a maximum substrate area for chemolithotrophic bacteria and algal species to act upon. A mechanical pulverizer is fed with the coal and steam. A sieve and a second tank receiving the coal from the pulverizer apparatus. An air exchanger connected to the second tank collects nanosized particulates of coal. A pipeline feeds the coal within the second tank with a mixture of chemolithophic bacteria from a breeding tank. A holding tank receives the mixture of coal and chemolithophic bacteria. A centrifuge receives the mixture of coal and chemolithophic bacteria from the holding tank and separates the coal from the mixture. A fourth tank receive the separated and hydrated coal particles from the centrifuge.

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 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”.

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.