Nozzle type centrifugal machine with improved slurry pumping chambers
AssigneeDorr-Oliver Incorporated
InventorsCharles Arthur Willus, Per Nyrop
Life of this patent
Estimating the term…
Loading patent…
AssigneeDorr-Oliver Incorporated
InventorsCharles Arthur Willus, Per Nyrop
Estimating the term…
A nozzle type centrifugal machine designed for two-fraction separation of feed slurry, wherein the rotor has a light fraction overflow at the top, while feed slurry as well as underflow return slurry from the nozzles are introduced into the rotor from below into respective feed accelerating pumping chambers, and wherein improvements in the pumping chambers results in reduced power requirement and in improved overall performance of the machine.
A nozzle type centrifugal machine adapted for a two phase separation of a feed slurry into a nozzle discharge slurry and an overflow of separated liquid,
A nozzle type centrifugal machine adapted for a two phase separation of a feed slurry into a nozzle discharge slurry and an overflow of separated liquid,
Dependencies are inferred from the claim text.
Drawings are temporarily unavailable. Open the PDF at USPTO
With discharging outlets in the plane of the maximum diameter of the bowl: with continuous discharge
Feeding, charging, or discharging bowls: arrangement of distributors or collectors in centrifuges
Centrifuges
Term ended 10 Jan 1995 (estimated)
USPTO file history isn’t available for this patent, so only indexed dates are shown.
This invention relates to centrifugal machines of the nozzle type wherein a double-cone shaped rotor bowl has a separating chamber containing a stack of separating discs for effecting a two-fraction separation of a feed slurry into a heavy nozzle discharge slurry or socalled underflow fraction or concentrate delivered by the nozzles, and a light fraction or separated liquid delivered by overflow from the top end of the machine. Provision is made for a part of the underflow fraction to be returned to the separating chamber at a controllable rate, by introduction through the lower end of the rotor bowl.
In the type of rotor embodying the invention, both the nozzle discharge return material and the feed slurry are introduced by injection upwardly into the rotor, and into respective annular pumping chambers located one above the other. These pumping chambers herein termed the pumping section of the rotor, deliver the respective slurries upwardly into the separating chamber in the rotor bowl.
The two pumping chambers communicate respectively with a set of upright slurry feed tubes delivering into the stack of separating discs in an inner separating zone, and with a set of outwardly divergent underflow return tubes delivering a portion of the nozzle discharge slurry into an outer annular separating zone which surrounds the discs in the rotor bowl.
FIG. 1 is a vertical sectional view of the rotor, embodying one form of the invention, wherein the upper and the lower pumping chamber are related to the vertical feed pipes and the divergent return pipes respectively in the rotor bowl.
FIG. 2 is a vertical sectional view of the rotor similar to FIG. 1, embodying a reversal of parts.
FIG. 3 is a cross-sectional view taken on line 3--3 in the FIG. 1 embodiment showing the relationship between the pumping vanes, the pipe system within the rotor bowl and the nozzles, in that embodiment. (Note: A similar cross-sectional view taken in FIG. 2 would be identical).
The centrifugal machine embodying one form of the invention in FIG. 1, is of the type constructed for a two phase separation of a feed slurry or solids suspension into the heavy fraction of a desired solids concentration, delivered by the rotor nozzles, and a light overflow fraction delivered at the top end of the rotor bowl. In this type of machine, feed slurry is introduced through the rotor bottom end, instead of downward through the top end of the rotor. Such bottom feed arrangement leaves the top overflow end unencumbered, thus avoiding what might be an undesirably large overflow diameter required for accommodating the top feed supply facilities.
Furthermore, since recirculation of a portion of the nozzle discharge product or underflow material back into the separating chamber of the rotor is normally required, provision is also made for the introduction thereof through the bottom end of the rotor into the outer centrifugal separating zone of the nozzles, that is the zone that surrounds the stack of separating discs.
The two slurries, that is the feed slurry and the return slurry to undergo separation, are pushed upwardly through the rotor by the pumping or impeller vanes of the respective annular pumping chambers. These pumping chambers presenting substantially identical pumping problems, occupy the smaller bottom end portion of the rotor, being located below the much greater centrifugal separating chamber or separating zones contained in the rotor bowl.