Various examples are provided in relation to improved recovery and throughput of both fine and coarse particulate materials. In one example, a method includes injecting an aqueous suspension of a cloud of small air bubbles into an aqueous phase including fine particulate materials, wherein the fine particulate material is selectively hydrophobized and collected by small air bubbles; allowing the bubbles to rise in the aqueous phase; and collecting the air bubbles to obtain a concentrate of the fine particulate materials. In another example, a method includes adding a hydrophobizing agent to an aqueous phase to render coarse particulate material selectively hydrophobic; allowing air bubbles to attach to the coarse particulate material and changing the apparent specific gravity of the coarse particulate materials so a layer of one type of coarse particle is formed on top; allowing the one type of coarse particles to float and enter the forth phase.

The present invention relates to apparatuses, systems, and methods to cleanse water contaminated with hydrocarbons, hydraulic fracturing fluids, volatile organic compounds, sulfurous compounds, crude oil, and other petroleum products. The products recovered with the invention can be returned to the source, stored, transported, sold, or otherwise reused.

The present invention relates to apparatuses, systems, and methods to cleanse water contaminated with hydrocarbons, hydraulic fracturing fluids, volatile organic compounds, sulfurous compounds, crude oil, and other petroleum products. The products recovered with the invention can be returned to the source, stored, transported, sold, or otherwise reused.

Apparatus and methods configured for cyclonic froth separation are disclosed. Exemplary implementations may: provide slurry into a first volute; provide fluid communication between the first volute and an interior of a porous barrier; receive pressurized gaseous fluid through a body wall to an exterior of the porous barrier; provide fluid communication between the exterior of the porous barrier and the interior of the porous barrier; facilitate flows of pressurized gas through the porous barrier; receive outputted froth and output froth to the exterior of the apparatus; provide fluid communication between the interior of the porous barrier and the second volute; retain froth within the interior of the porous barrier; receive slurry exhausted from the interior of the porous barrier; provide fluid communication of exhausted slurry to the exterior of the apparatus.

Disclosed is a vortex mineralization-static separation flotation device and a flotation method. The device comprises: a static separator provided with a separation chamber and a vortex mineralizer provided with a mineralization cylinder. The separation chamber includes a raw ore treatment pipeline and an intermediate ore treatment pipeline. The mineralization cylinder includes a vortex mineralization pipeline. The method comprises: the mineralization cylinder being full of a raw ore slurry and the raw ore slurry in the separation chamber reaching a set level, turning on air conduits and an agitation device to make air enter the mineralization cylinder and form tiny bubbles to collide with first mineral particles and mineralize to form an aerated intermediate ore slurry; the aerated intermediate ore slurry entering the separation chamber and performing collision and mineralization with second mineral particles and the raw ore slurry, and concentrate froth being formed at a top of the separation chamber to be collected.

The embodiments disclose a hydrocyclone apparatus for separating particles from a slurry including a central body wall extending from a first opening at one end to a second opening at the opposite end, an air base column coupled to the second opening configured to support the hydrocyclone, at least one slurry from a group of containing water with solid particles, hydrophobic particles, or saltwater particles configured to be flowed into the hydrocyclone apparatus, a first volute coupled to the first opening slurry input port configured to allow slurry to flow from the volute into the central body, an overflow opening coupled to the first opening configured to recover separated water and hydrophobic particles, a second volute coupled to the second opening exhaust port configured to allow slurry to exit the central body, and a plurality of underflow exit openings coupled to the exhaust port that expel particles from the apparatus.