Abstract: The present invention discloses a high-speed counter-current chromatograph unreeled by a gear ring, including an upper disc, a middle disc and a lower disc, wherein an unreeling gear ring coaxial with the middle disc is fixed above the middle disc, the lower disc is driven by a driving shaft to rotate, the unreeling gear ring is fixed, gear teeth of the unreeling gear ring are distributed on the inner ring thereof, multiple groups of gears engaged with the unreeling gear ring are arranged along the circumferential direction of the inner ring of the unreeling gear ring, gears between the adjacent groups are not engaged with each other, each group of gears includes two gears that are engaged with each other, wherein one gear drives a separation column, the other gear drives an unreeling shaft, the separation column is installed on a separation shaft, the upper ends of the unreeling shaft and the separation shaft are connected with the upper disc, and the lower ends are connected with the middle disc; meanwhile,

Abstract: An embodiment comprises a container to include a substrate during processing (e.g., centrifugal or vibratory processing) and protect the substrate from other substrates (e.g., medical implants) that are simultaneously being processed and/or from the polishing environment (e.g. vibratory tub sidewalls) during processing. Other embodiments are described herein.

Abstract: A shaker for separating solids from a drilling fluid includes a top screening deck (130), a flow-back pan (160) positioned beneath the top screening deck (130) for receiving an initially separated drilling fluid from the top screening deck. The flow-back pan (160) is divided into a plurality of channels (A, B, C, D). The shaker further includes a fluid distribution box (210), which includes a plurality of conduits (A, B, C, D). Each channel (A, B, C, D) of the flow-back pan (160) corresponds to one of the plurality of conduits (A, B, C, D) in the fluid distribution box (210) and each channel communicates a stream of the initially separated drilling fluid to the corresponding conduit. The shaker further includes a middle screening deck (140) and a bottom screening deck (150). Each conduit (A, B, C, D) routes the stream of initially separated drilling fluid to a corresponding one of the middle screening deck (140) and the bottom screening deck (150).

Abstract: Certain examples describe systems and methods for increasing plasma extracted from donor blood. An example method includes receiving blood extracted from a donor connected to a blood collection machine. The example method includes filtering the blood using a filtration device to remove at least a portion of plasma included in the blood to separate the plasma removed from remaining blood. The example method includes routing the plasma removed for collection. The example method includes re-filtering the remaining blood using a or the filtration device to remove additional plasma from the remaining blood. The example method includes routing the additional plasma removed for collection.

Abstract: A melt filter, for the purification of plastic melts, particularly dispensed from extruders, comprises a housing (1) with a melt channel (10), connecting a melt inlet (7) to a melt outlet (9), with a sieve disc (5), which may be rotated by a motorized ratchet drive provided in the melt channel (10), comprising recesses separated by ridges in a circular track for housing exchangeable filter elements and the housing (1) has a filter element changing station (13). The aim of the invention is that the above shall be designed such that large amounts of melt for filtering can be filtered in a cost-effective energy saving and space saving manner. The above is achieved by means of the housing comprising at least two melt inlets (7, 8) connected to the melt outlet (9) by at least two melt channels (10, 11) and in each melt channel (10, 11) a sieve disc (5, 6) driven on rotation by a motorized ratchet drive is provided and each sieve disc (5, 6) is provided with a filter element exchange station (13, 15).

Abstract: For separating solids contents from a pulp, the pulp is concentrated in a filter device by intense movement up to a predetermined solid matter content. In the filter device, the dynamic pressure and Venturi effects are utilized to support the filtering process. During the discharge of the filtrate, pulp is supplied to keep the filter device in filled condition. The concentrated pulp is batch-wise transferred into a pressing chamber in which the discharged batch is mechanically pressed-out. The pressing cake generated thereby is mechanically comminuted.

Abstract: A shale shaker having two feeds, two screens, two mud outlets and a removable tray between the screens is disclosed. Each screen receives one feed and produces one outlet of cuttings and another outlet for separated mud for either bypass or direct feed to the mud tank or the other screen. The removable tray or trays facilitate the two screens acting in cascade. Valves are provided to control the overall flow rate to the shaker and to the lower level screen.

Abstract: A liquid sample filtration apparatus includes: a) a module retaining filter elements; b) a filter clamping and fluid injection apparatus positioned relative to the module to engage a filter element thereon, and includes a pair of first and second opposing engageable members to sealing engage a filter element therebetween; c) an inlet tube connected to an opposing engageable member; d) an outlet tube connected to an opposing engageable member; e) a motor to move the module relative to the filter clamping and injection apparatus to register filter elements on the module to the clamping and injection apparatus; and f) a motor associated with the filter clamping and injection apparatus to move the opposing engageable members into substantial sealing fluid communication relative to a filter element on the module.

Abstract: An apparatus for separating a component from a liquid is disclosed herein. The apparatus includes a plurality of cartridges disposed within a tank, the cartridges being mounted on a support member rotatable about a first axis, and each cartridge being rotatable about a second axis parallel to the first axis. The cartridges include a plurality of holes on an outer periphery thereof, and contain a supply of a granular ion exchange material capable of separating a desired component from the liquid. Means are provided for transferring liquid to be separated into the tank, and to discharge treated liquid from the cartridges to a location outside the tank.

Abstract: Separating elements (14) arranged about a central shaft (1a) rotate in common about the main axis (A) and individually about their longitudinal axes (B). A centrifugal distributor (6) distributes fine-grain mineral mixture mixed with fluid uniformly to the separating elements (14). In each separating element (14) the partial material flow (2a) is set in rotation about the longitudinal axis (B) by entrainment vanes (18) arranged in a first separating element section (15a) and the heavy fraction is centrifuged on to the separator wall (16a). In the second section (15b), formed as conical tubular worm conveyor, which contains no entrainment vanes, the heavy fraction is transported to the collecting chamber (21) and discharged through first discharge openings (22), the fine-grain mineral mixture being fluidized in pulsation on the separating wall (16b) by the combined rotating movements and the heavy fraction being concentrated.

Abstract: A pocket centrifuge has a plurality of sieve pockets having sieve surfaces and orbitable about an axis with the sieve surfaces forming sieve angles with perpendiculars to planes including this axis. A filtrant is fed radially to these pockets so that solids collect on the surfaces thereof and a filtrate passes through the surfaces. These solids have a friction angle measured to a perpendicular to the centrifugal force acting on them which is dependent on the magnitude of this force and their coefficient of friction. The angular orbiting speed of the pocket is periodically varied between one speed at which the respective friction angle of the solids is smaller than the sieve angle and the solids slide on the sieve surface and another angle at which the respective friction angle of the solids is greater than the sieve angle and the solids sit on the sieve surface.

Abstract: Apparatus for separating liquid from solids contained in a liquid-solid slurry includes a centrifugal concentrator which is supplied with feed slurry, and a centrifugal separator to which the output of the concentrator is conducted. The concentrator includes a rotatable central slurry reservoir having outlets discharging slurry under centrifugal force in streams nominally following spiral flow paths. Spirally-curved perforate vanes rotated with the reservoir and intersect respective slurry streams at acute angles. A fractional portion of the fluid in the slurry is removed by filtration as each stream intersects and then flows along a spirally-curved perforate vane, thereby to provide concentrated slurry, which is supplied to the separator. The separator includes a high-speed rotatable carrier, which carries eccentrically-disposed filter baskets independently rotatable at low speeds about their own axes.

Abstract: A rotary filter has a pressure vessel and a rotor from which a plurality of filter cells are suspended from outer portions of the rotor so that they clear a conveyor located proximal to the axis of rotation and upon which the filter cake is removed. Conduits are connected to the filter cells from a single distribution head for initially evacuating the cells in the filter stage and thereafter pressurizing the cells to dislodge the filter cake while the vessel remains under pressure. The filter cells can have the filter surfaces extending generally in axial planes or in axially spaced relationship in planes wherein a plurality of angularly spaced filters extend generally radially from respective filtrate conduits running axially along the outer part of the rotor.

Abstract: A flow-through coil planet centrifuge mechanism with variable rotation-revolution (r/R) speed ratios, which does not employ rotating seals. The rotation and revolution rates are continuously adjustable by using separate variable-speed drive motors. A system of gearing and belts compensates for the rotation and revolution of the centrifuge column relative to a stationary supporting frame structure to avoid twisting of the flow tubes. A first motor drives a pair of spider assemblies arranged coaxially with a column-supporting spool. One spider assembly has planetary gearing cooperating with a fixed gear belt to rotate the column relative to the spool. The other spider assembly has planetary gearing driven by a second motor and coupled to the column support spool so that the spool revolves relative to the stationary frame structure and simultaneously the column rotates relative to the spool.

Abstract: An apparatus for filtering liquids comprises a substantially cylindrical shaped and horizontally placed filter-casing in which at least one supporting member is journaled for rotation substantially about the axis of the casing. The supporting member is provided with a number of hollow rotating shafts, evenly spaced around its axis of rotation, and each shaft carries at least one disc-shaped filter-element. The filtrate discharge from the disc-shaped filter elements passes through the hollow rotating shafts to an outlet-conduit mounted stationary with respect to the supporting member. A conveying trough provided with a conveying screw is arranged substantially in aligmment with the axis of rotation of the supporting member to transport the filter-cake dislodged from the filter-elements and received by the trough out of the filter-casing.

Abstract: The subject of the invention is a continuous filtering-settling centrifuge designed for separating continuously mixtures containing solid and liquid bodies.In the centrifuge several filtering or settling baskets are applied, situated beyond the main axis of spinning, and rotating around their own axes at an angular velocity different from the angular velocity of the centrifuge. In the particular filtering or settling baskets there is applied a system of feeding the mixture to be centrifuged, constituting a separated feeding zone, and a discharge system constituting a separate discharge zone with a chute receiver or a worm receiver. Besides, in the particular baskets there are separated zones of centrifuging, washing the solid part with a liquid, steaming of the solid part, separating of the washing agent or steaming agent, drying of the solid part, and washing of filtering screens with appropriate technical means in the particular zones. In the baskets finned partitions are applied.

Abstract: A continuous discharge centrifuge for material of any nature, and particularly suitable for fibrous materials comprising a rotating structure, a filtering surface associated with it and provided with its own drive, and disposed without discontinuity along essentially annular and substantially concentric paths, means for moving said filtering surface along the paths relative to the rotating structure, and systems located within the internal path for feeding the material to be centrifuged on to the filtering surface.

Abstract: A filter comprising a vessel in the form of a closed drum which is rotatably mounted about a horizontal central axis, and a plurality of longitudinal, hollow, horizontal filter elements which are arranged in a ring. The filter elements extend between and are connected to the end walls of the drum for rotation about the central axis together with the drum. The peripheral surfaces of the filter elements constitute a filter surface which, upon rotation of the drum and the elements, will submerge into and emerge from the liquid to be filtered which is contained in the drum. At one end the filter elements extend through the end wall of the drum, and this end of the filter elements is open to permit unobstructed discharge of the filtrate. A blow tube with nozzle means is provided within each filter element, with the blow tube serving to remove solids deposited on the filter surface when the surface is above the liquid level in the vessel.