Abstract: 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.

Abstract: 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.

Abstract: 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.

Abstract: 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.

Abstract: According to some examples, solutions are provided for setting a cooling system of a computer system chassis by a positionable cover disposed on a computer hardware component receivable by the computer system chassis.

Abstract: According to some examples, solutions are provided for setting a cooling system of a computer system chassis by a positionable cover disposed on a computer hardware component receivable by the computer system chassis.

Abstract: A heat exchanger including a first plate and a second plate spaced apart from the first plate that defines a first gap between inner surfaces of the first plate and the second plate in which a first fluid circulates, where a major portion of the first gap is free of obstructions, where a second fluid contacts an outer surface of the first or second plate for heat exchange with the first fluid, where a first peripheral wall on the periphery of the first gap has a curved profile inside the first gap, and at least one inlet is radially positioned with respect to the first gap and injects the first fluid in the gap, and least one outlet is centrally positioned in one of the first and the second plate to enable the first fluid to exit the first gap, where first fluid circulates in a swirling flow in the major portion of the first gap.

Abstract: A heat exchanger including a first plate and a second plate spaced apart from the first plate that defines a first gap between inner surfaces of the first plate and the second plate in which a first fluid circulates where a major portion of the first gap is free of obstructions, where a second fluid contacts an outer surface of the first or second plate for heat exchange with the first fluid, where a first peripheral wall on the periphery of the first gap has a curved profile inside the first gap, and at least one inlet is radially positioned with respect to the first gap and injects the first fluid in the gap, and least one outlet is centrally positioned in one of the first and the second plate to enable the first fluid to exit the first gap, where first fluid circulates in a swirling flow in the major portion of the first gap.