← Back to Patent Explorer
US3642129A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus and method for continuously separating solid particles in a fluid medium

Assignee: SOUTHWEST RESOURCES Inc
•
Filing: 1969-09-19
•
Granted: 1972-02-15
•
Expires: 1989-09-19
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Classification apparatus for continuously separating solid particles in a fluid medium contained in a cylindrical vessel. Upwardly and downwardly spiraling vortices of turbulence are created in the fluid medium by injecting pressurized fluid streams through the sides of the vessel. A mixture of the particles and fluid medium are introduced downwardly through the top of the vessel to intercept the upwardly spiraling vortex and causing a first separation of heavy and light particles, the heavier particles falling down through the fluid medium and intercepting the downwardly spiraling vortex and effecting a second separation of heavy and light particles. The lighter particles are swept upwardly and discharged by the action of the fluid medium and the heavy particles are discharged through the bottom of the vessel.

Inventors

  • 👤 Philip F Mcdaniel
  • 👤 Lonnie Dee Kirby

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 18:14
CPC Classifications
B; B03; B03B; B03B5/00; B03B5/62; B03B5/623

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 45 words
The nozzles of said first group of nozzles as described in claim 1 are positioned upwardly at a 45* angle from the horizontal and at a 15* angle from the vertical for accomplishing the creation of an upwardly, inwardly and circularly swirling area of turbulence.
Claim 2
Dependent Claim 45 words
The nozzles of said second group of nozzles as described in claim 1 are positioned downwardly at a 45* angle from the horizontal and at a 15* angle from the vertical for accomplishing the creation of a downwardly, inwardly and circularly swirling area of turbulence.
Claim 3
Dependent Claim 439 words
Apparatus for continuously separating discrete particles having varying specific gravities and resistances to fall in water as a separating medium, comprising an elongated cylindrical vessel vertically oriented for receiving the water and particles and forming a separation chamber for the particles, said vessel being closed at the loweR end by downwardly and inwardly depending walls for forming a particle settling chamber having a downwardly directed aperture coaxial with the vertical axis of said vessel, overflow means peripherally disposed adjacent the topmost portion of said separation chamber and communicating interiorly therewith, a conduit fixed to the closed top of said vessel and concentrically projecting downward into said separating chamber for continuously introducing a mixture of the water and discrete particles downwardly into said separation chamber, a manifold encircling the outer periphery of said vessel and attached thereto adjacent the lower end of said separation chamber, said manifold having first and second chambers for carrying water under pressure, a first group of horizontally disposed, spaced nozzles fixed to the interior periphery of said vessel opposite one of said encircling manifold chambers, and communicating with said chamber carrying the water under pressure, said first group of nozzles angled with respect to the radial direction for directing the pressured water upwardly, inwardly and circularly into said separation chamber for forming an upwardly spiraling area of turbulence and imparting an upward rotational motion to the water within said separating chamber, the axis of rotation of the water being substantially coincident with the vertical axis of said vessel, said upwardly spiraling area of turbulence in the water effecting a first separation of the particles having a lesser specific gravity and a greater resistance to fall from the particles having a greater specific gravity and a lesser resistance to fall, the lighter particles being swept upwardly for discharge through said overflow means and the heavier particles settling down into said settling chamber, a second group of horizontally disposed, spaced nozzles fixed to the interior periphery of said vessel below said first group opposite said encircling second manifold chamber and communicating with said second chamber carrying the water under pressure, said second group of nozzles angled with respect to the radial direction for directing the pressurized water downwardly, inwardly and circularly into said settling chamber for forming a downwardly spiraling area of turbulence to sweep the inner surface of said settling chamber and effecting a second separation of the particles having a lesser specific gravity and a greater resistance to fall from the particles having a greater specific gravity and a lesser resistance to fall and carrying the heavier particles into said settling chamber aperture for discharge.
Claim 4
Dependent Claim 26 words
The nozzles of said first group of nozzles as defined in claim 4 are angled inwardly and upwardly at preselected angles to the horizontal and vertical.
Claim 5
Dependent Claim 26 words
The nozzles of said second group of nozzles as defined in claim 4 are angled inwardly and downwardly at preselected angles to the horizontal and vertical.
Claim 6
Independent Claim 257 words
A method for continuously separating discrete particles within a vessel having varying specific gravities and resistances to fall in water as a separating medium, comprising the steps of creating an upwardly spiraling conical area of turbulence in the water within the vessel for imparting rotational motion to the fluid medium, simultaneously creating a downwardly spiraling conical area of turbulence in the water within the vessel below said upwardly spiraling conical area of turbulence for imparting rotational motion to the water complementary to the rotational motion caused by said upwardly spiraling area of turbulence, and introducing a mixture of the particles and water into the vessel along the rotational axis of said upwardly and downwardly spiraling areas of turbulence and above the apex of said upwardly spiraling area of turbulence to intercept said rotating water and said upwardly spiraling area of turbulence for effecting a first separation of the particles having a lesser specific gravity and a greater resistance to fall from the particles having a greater specific gravity and a lesser resistance to fall, the lighter particles being swept upwardly for discharge from the vessel and the heavier particles settling down through said upwardly spiraling area of turbulence in the rotating column of water for interception by said downwardly spiraling area of turbulence for effecting a second separation of the particles having a lesser specific gravity and a greater resistance to fall from the particles having a greater specific gravity and a lesser resistance to fall and carrying the heavier particles downward for discharge from the vessel.

References Cited (Backward Citations)

CA536384A Cited
US654647A Cited
FR348958A Cited
US982583A Cited
US1937190A Cited
US2150226A Cited
US2172792A Cited
US2967617A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-02-14 1975-08-16 1976-02-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-02-14 1979-08-16 1980-02-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-02-14 1983-08-16 1984-02-15 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag