Abstract: A centrifuge of the type having a rotary basket with a bottom wall, side wall and a top wall with a central opening therein includes a liquid feed pipe extending into the basket through the top opening to a point spaced above the basket bottom wall at the rotary axis thereof for conducting a feed liquid into the basket. A feed accelerator projects from the basket bottom wall opposite the feed pipe. The accelerator rotates with the basket so that, the accelerator will impart radial and angular acceleration to the liquid issuing from the feed pipe so that that liquid is redirected and accelerated toward the basket side wall. The centrifuge also incorporates a liquid drain in the basket bottom wall adjacent to the rotary axis of the basket for draining liquid from the basket when the rotation of the basket is stopped.

Abstract: In centrifuges for separating solids-liquid slurries and which discharge concentrated solids through nozzles at the periphery of the centrifugal bowl or rotor, it is necessary to maintain a feed or influent rate at least as great as the nozzle discharge rate. According to the present invention, this is accomplished by driving from the centrifuge drive train a pumping means for returning concentrated solids from the nozzles to the centrifuge for recycling through the bowl.

Abstract: In a centrifuge for the separation of solids from liquid in which concentrated solids are discharged from radial nozzles at the rotor periphery, there is a need for control of the solids concentration by controlling the recycle of solids to the centrifuge. The present invention provides a flow path divided into small cross-sectional areas, as with parallel plates, for the flow of recycled solids therethrough, at an appropriate pressure drop and flow rate to cause a strong dependence on fluid viscosity. A small receiving tank, with a fixed or adjustable weir, is attached to the inlet of the sectional flow path to provide a constant pressure drop through the device by maintaining a volume of concentrated solids at a pre-selected height above the inlet. The cross-sectional area available for flow is manually adjustable by means of a blocking plate at the inlet of the sectioned flow path.