US431313A - Pneumatic ore-concentrator - Google Patents

Pneumatic ore-concentrator Download PDF

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US431313A
US431313A US431313DA US431313A US 431313 A US431313 A US 431313A US 431313D A US431313D A US 431313DA US 431313 A US431313 A US 431313A
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pipe
ore
concentrator
hood
pneumatic
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B4/00—Separating solids from solids by subjecting their mixture to gas currents
    • B07B4/02—Separating solids from solids by subjecting their mixture to gas currents while the mixtures fall

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  • Pueblo in the county of Pueblo and State of lolorado, have invented a new and Improved Pneumatic Ore 4 Concentrator, of which the following is a full, clear, and exact description.
  • the object of the invention is to provide a new andimproved ore-concentrator which is simple and durable in construction, very effective in operation, and specially designed to concentrate by means of an exhaust-blastpulverized ores, such as are usually passed through water-jigs.
  • Figure 1 is a sectional side elevation of the improvement.
  • Fig. 2 is a sectional-view of the same on the line 00 o: of Fig. 1
  • Fig. 3 is an enlarged sectional plan view of part of the improvement on the line y y of Fig. 1.
  • Theimproved ore-concentrator is provided with a hopper A, into which the pulverized ores to be treated are placed. 011 the lower end of the hopper A are arranged suitable slides B, opening into a pipe 0 and serving to regulate the amount of pulverized ores passing from the hopper A into the pipe 0.
  • the lower end of the pipe O discharges onto a body D, suspended by rods E in a -chamber F of.a vertical pipe F, opening at its lower end into the outer air and provided at its upper end with an outwardly-curved flange F the top of which extends to within a short distance of the lower end of the pipe 0.
  • the body D may be circular or elliptical, as shown, the chamber F being correspondinglyshaped, there being enough room between the outer surface of the body D and the inner surface of the chamberF to permit the valuable metals to pass down into the lower part of the pipe F.
  • annular hood G On the lower end of the pipe 0 is secured an annular hood G, arranged over the annular flange F, as is plainly shown in Fig. 1.
  • the pipe O, the hood G, and part of the pipe F, with the body D, are inclosed in an airtight easing I-I, provided in its lower end with a funnel II, from which opens an outlet 1, adapted to be opened and closed by a slide J.
  • the upper end of the casing H connects with a channel or pipe K, connected with an exhaustfan of any approved construction.
  • a valve L for regulating the exhaust-blast.
  • the operation is as follows: When the exhaust-fan is set in motion, a current of air is drawn from the outside through the pipe F, over the annular flange F is guided downward by the hood G, and then passes up into the channel K and to the exhaust-fan.
  • the ore to be treated is previously sized by suitable means, is passed into the hopper A, and descends through the pipe 0 into the upper end of the pipe F, striking onto the body D, so that the ore is distributed all around, giving the air-blast a chance to act on all the distributed particles.
  • the object in having the capacity of the overflow the same as that of the airspace in the chamber F is that particles heavy enough to fall against the pressure of air surrounding the body shall not be carried over, and that any particles not heavy enough to fall against said pressure shall be carried over and not remain in the separating-chamber.
  • a pneumatic ore-concentrator the combination, with a pipe opening at one end into the outer air and provided at its other end with an annular curved flange, of a body suspended in the said pipe, a feed-pipe opening onto the said body and carrying a hood held over the said annular flange, a casing inclosing the said feed-pipe, hood, and body and connected with an exhaust-fan, and a hopper provided with slides which regulate the flow of ore to the said feed-pipe, substantially as shown and described.

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  • Manufacture And Refinement Of Metals (AREA)

Description

(No Model.)
O.BALLARD. PNE UMATIG ORE OONGENTRATOR.
No. 431,313. Patented July 1, 1890.
ATTORNEYS.
Tans cu., mom-mum, wxsumm-ou, n. c,
UNITED STATES PATENT ()FFICE.
CHARLES BALLARD, OF PUEBLO, COLORADO.
PNEUMATIC ORE-CONCENTRATOR.
SPECIFICATION forming part of Letters Patent No. 431,313, dated July 1, 1890.
Application filed November 15, 1889. Serial No. 330,408. (No model.)
To ctZZ whom it may concern.-
Be it known that I, CHARLES BALLARD, of
Pueblo, in the county of Pueblo and State of lolorado, have invented a new and Improved Pneumatic Ore 4 Concentrator, of which the following is a full, clear, and exact description.
The object of the invention is to provide a new andimproved ore-concentrator which is simple and durable in construction, very effective in operation, and specially designed to concentrate by means of an exhaust-blastpulverized ores, such as are usually passed through water-jigs.
The invention consists of certain parts and details and combinations of the same, as will be hereinafter fully described, and then pointed out in the claims.
Reference is to be had to the accompanying drawings, forming a part of this specification, in which similar letters of reference indicate corresponding parts in all the figures.
Figure 1 is a sectional side elevation of the improvement. Fig. 2 is a sectional-view of the same on the line 00 o: of Fig. 1, and Fig. 3 is an enlarged sectional plan view of part of the improvement on the line y y of Fig. 1.
Theimproved ore-concentrator is provided with a hopper A, into which the pulverized ores to be treated are placed. 011 the lower end of the hopper A are arranged suitable slides B, opening into a pipe 0 and serving to regulate the amount of pulverized ores passing from the hopper A into the pipe 0. The lower end of the pipe O discharges onto a body D, suspended by rods E in a -chamber F of.a vertical pipe F, opening at its lower end into the outer air and provided at its upper end with an outwardly-curved flange F the top of which extends to within a short distance of the lower end of the pipe 0. The body D may be circular or elliptical, as shown, the chamber F being correspondinglyshaped, there being enough room between the outer surface of the body D and the inner surface of the chamberF to permit the valuable metals to pass down into the lower part of the pipe F.
On the lower end of the pipe 0 is secured an annular hood G, arranged over the annular flange F, as is plainly shown in Fig. 1.
The pipe O, the hood G, and part of the pipe F, with the body D, are inclosed in an airtight easing I-I, provided in its lower end with a funnel II, from which opens an outlet 1, adapted to be opened and closed by a slide J.
The upper end of the casing H connects with a channel or pipe K, connected with an exhaustfan of any approved construction. In the channel or pipe K is held a valve L for regulating the exhaust-blast.
The operation is as follows: When the exhaust-fan is set in motion, a current of air is drawn from the outside through the pipe F, over the annular flange F is guided downward by the hood G, and then passes up into the channel K and to the exhaust-fan. The ore to be treated is previously sized by suitable means, is passed into the hopper A, and descends through the pipe 0 into the upper end of the pipe F, striking onto the body D, so that the ore is distributed all around, giving the air-blast a chance to act on all the distributed particles. Particles heavy enough to fall against the blast surrounding the body D descend and are discharged through the pipe F, while the lighter particles are carried up by the blast and are thrown over the annular flange F against the hood G, to be pressed downward, so that the lighter particles or tailings settle in the hopper H, from which they can be drawn olt' at suitable intervals through the inlet I by opening the slide J. The air alone passes upward into the channel K, as previously described. Now it will readily be seen that no power is needed .to handle the heavy particles of ore, as they fall by their own weight, sufficient blast to carry off the light material being all that is necessary. The space between the flange F and the hood G should be of the same size as the space surrounding the body D in the chamber F. The object in having the capacity of the overflow the same as that of the airspace in the chamber F is that particles heavy enough to fall against the pressure of air surrounding the body shall not be carried over, and that any particles not heavy enough to fall against said pressure shall be carried over and not remain in the separating-chamber.
Having thus fully described my invention, I
claim as new and desire to secureby Letters Patent-r 1. Ina pneumatic ore-concentrator,the combination, with a pipe opening at one end into the outer air and provided at its other end the outer air and provided at its other endwith an annular curved flange, of a body suspended in the said pipe, a feed-pipe opening onto the said body and carrying a hood held over the said annular flange, and a casing inclosing the said feed-pipe, hood, and body and k connected with an exhaust-fan, substantially as shown and described.
3. In a pneumatic ore-concentrator, the combination, with a pipe opening at one end into the outer air and provided at its other end with an annular curved flange, of a body suspended in the said pipe, a feed-pipe opening onto the said body and carrying a hood held over the said annular flange, a casing inclosing the said feed-pipe, hood, and body and connected with an exhaust-fan, and a hopper provided with slides which regulate the flow of ore to the said feed-pipe, substantially as shown and described.
CHARLES BALLARD.
, Witnesses:
G. H. HARD,
W. P. HARD.
US431313D Pneumatic ore-concentrator Expired - Lifetime US431313A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3833117A (en) * 1973-01-29 1974-09-03 New Life Foundation Pneumatic refuse material separation system
US4834544A (en) * 1987-07-06 1989-05-30 Fuller Company Fines separation system for pellet blender
US20080130399A1 (en) * 2006-11-14 2008-06-05 Rensselaer Polytechnic Institute Methods and apparatus for handling or treating particulate material
US20130017326A1 (en) * 2006-11-14 2013-01-17 Rensselaer Polytechnic Institute Methods for coating particulate material

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3833117A (en) * 1973-01-29 1974-09-03 New Life Foundation Pneumatic refuse material separation system
US4834544A (en) * 1987-07-06 1989-05-30 Fuller Company Fines separation system for pellet blender
US20080130399A1 (en) * 2006-11-14 2008-06-05 Rensselaer Polytechnic Institute Methods and apparatus for handling or treating particulate material
US7621668B2 (en) * 2006-11-14 2009-11-24 Rensselaer Polytechnic Institute Methods and apparatus for handling or treating particulate material
US20130017326A1 (en) * 2006-11-14 2013-01-17 Rensselaer Polytechnic Institute Methods for coating particulate material
US8557336B2 (en) * 2006-11-14 2013-10-15 Rensselaer Polytechnic Institute Methods for coating particulate material

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