US1715693A - Ore classifier - Google Patents
Ore classifier Download PDFInfo
- Publication number
- US1715693A US1715693A US170977A US17097727A US1715693A US 1715693 A US1715693 A US 1715693A US 170977 A US170977 A US 170977A US 17097727 A US17097727 A US 17097727A US 1715693 A US1715693 A US 1715693A
- Authority
- US
- United States
- Prior art keywords
- chamber
- water
- coal
- container
- floor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 239000003245 coal Substances 0.000 description 13
- 238000005192 partition Methods 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 239000002245 particle Substances 0.000 description 10
- 238000000926 separation method Methods 0.000 description 5
- 239000012535 impurity Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/02—Washing granular, powdered or lumpy materials; Wet separating using shaken, pulsated or stirred beds as the principal means of separation
- B03B5/10—Washing granular, powdered or lumpy materials; Wet separating using shaken, pulsated or stirred beds as the principal means of separation on jigs
- B03B5/22—Washing granular, powdered or lumpy materials; Wet separating using shaken, pulsated or stirred beds as the principal means of separation on jigs using pulses generated by liquid injection
Definitions
- This invention relates to an improvement in ore classifiers constructed and arranged to subject the material to successive currents of water of increasing strengths to compel the desired separation.
- the feed usually has received, previously, some preliminary treatment such as screen-sizing in which the coal particles, which are of lower specific gravity than the impurities, are so prepared that they are not above a certain number of times the diameter of the refuse particles from which they must be separated,
- the relative size of coal and refuse particles which can be separated in the apparatus and prepare finished products depends upon hindered-settling ratios of the two materials which in turn depends chiefly on the relative specific gravity and shape of the particles;
- Figure l is a plan view of the improved classifier.
- Figure 2 is a vertical section on the line 2-2 of Figure 1.
- Figure 3 is a broken sectional view on the line 3-3 of Figure 1.
- Figure 4 is an end elevation of the classifier.
- the improved classifier comprises a boxlike tank 1 of appropriate area divided. transversely by a partition 2, hereinafter termed the floor, which is inclined downwardly in the direction of feed of the material, the tank below the partition being a series of separating or classifyingchambers 8, 9, 10 and 11 by partitions 12. These partitions extend to and are secured to the side walls of the tank but terminate above the floor, leaving communicating passages 13 between the respective chambers.
- a sup ply pipe 14 leads beneath the tank and has outlets 15, 16, 17 and 18 communicating With the respective chambers 3, 4, 5 and 6, each outlet being controlled by a valve 19.
- the floor is perforated at 20 to permit the water rising in the chambers below the floor to geach the classifying chambers above the oor.
- the classifying chamber 8 is the initial receiving chamber and arranged on one side of the tank at the upper end is a feeder 21 into which material to be classified is placed,
- each classifying chamber is provided with a launder indicated at 23, and the sidewall defining the particular classifying chamber is of reucked height to permit the overflow to reach the launder.
- the side walls of the respective classifying chambers terminate at successively increasing heights in the direction of feed of the material, as indicated at 24 in Figure 3.
- a receiver 25 is secured to the end wall of the tank beyond the final classifying chamber 11 and formed with a discharge 26 for the delivery of the material.
- the end Wall of the tank between the final chamber 11 and the receiver 25 is of reduced height to provide a passage 27 in which the material from the final chamber can reach the receiver.
- the valves 19 controlling the outlets 15, 16, 17 and 18 have been opened to a degree to permit currents of Water of increasing intensity to flow through the respective chambers 3, 4, 5 and 6.
- the water rising through the perforated floor of the initial classifying chamber 8 separates such lighter particles ticular force, and de 'vers the same to the launder 23 connected with that chamber.
- the pressure of water in each of the classifying chambers may be adjusted by manipulation of the respective valvesto gain that force required for the particular separation.
- the number and size of the perforations 20in the floor are determined by the well established principles of hydraulics.
- the volume of water required to' maintain in a condition of teeter, the material in any given compartment may be determined by experiment. I
- the total area of the orifices under any given subchaniber is calculated to deliver the required quantity'of water under that head, and the size and number of orifices selected to suit the convenience of the operator, uniformly spaced apart in the screen. If the apparatus be large, it is preferred to graduate the size of orifices to compensate for the greater head toward the left half of any subchamber, as viewed in Figure 2.
- the different products and water are discharged into dewatering boxes in any approved manner, the excess of water overflowing the upper edge of the dewatering boxes. Excess water above that required for the subsequent disposition of the products of the apparatus may be removed in dewatering boxes, dewatering elevators or any other suitable apparatus common to the industry.
- a classifier In a classifier, the combination of a fixed container, a perforated partition arranged transversely and obliquely of the container and which divides the container into an upper and lower chamber, 'a pluralit of vertically arranged partitions WhlCh dlVldG the uppermost part .of the container into a plurality of upper sub-chambers, each subchamber being comparatively long transversely of the container and comparatively short longitudinally thereof, means for feeding the material to the first sub-chamber at one end thereof adjacent a corner of the container, the said vertical partitions being spaced away from the perforated partition, thus leaving a transverse sub-chamber having an oblique floor, the end wall of the container forming one wall of the last vertical chamber terminating short of the top edge of said container to form an overflow passage for the material, a separate receiving chamber with which the overflow passage connects, a side refuse chamber communicating with each vertical chamber at different distances from the top of the container, an additional group of vertically arranged partition
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Description
June 4, '1929. v B. M. BIRD 1,715,693
' ORE CLASSIFIER Fil ed Feb. 25, 1927 2 Sheets-Sheet 2 INVEINTOR 5 M57E0 BY Z W ATTORNEY BYRON M. BIRD, OF SEATTLE, WASHINGTON.
ORE CLASSIFIER.
Application filed February 25, 1927. Serial No. 170,977.
This invention relates to an improvement in ore classifiers constructed and arranged to subject the material to successive currents of water of increasing strengths to compel the desired separation.
In the present embodiment of my invention I will illustrate the invention in the classification of coal. The separation is effected between the coal and particles of impurities by a continuous uprising current of water according to established principles of ore dressing and coal washing, either in the separation of coal sons to fit itfor a subsequent treatment on coal washing tables, or in the preparation of coal in final products, washed coal, middlings and refuse. In the former, unsized coal, usually smaller than would be retained by a threerquarter inch screen, is fed into the apparatus, which separates the coal into its products commonly known in the art as classified. These classified products may be sufficiently free from impurities to suit the market requirements but usually they will require a further treatment on coal washing tables. In the latter application the feed usually has received, previously, some preliminary treatment such as screen-sizing in which the coal particles, which are of lower specific gravity than the impurities, are so prepared that they are not above a certain number of times the diameter of the refuse particles from which they must be separated, The relative size of coal and refuse particles which can be separated in the apparatus and prepare finished products depends upon hindered-settling ratios of the two materials which in turn depends chiefly on the relative specific gravity and shape of the particles;
The invention is illustrated in the accompanying drawings in which: I
Figure l is a plan view of the improved classifier.
Figure 2 is a vertical section on the line 2-2 of Figure 1.
Figure 3 is a broken sectional view on the line 3-3 of Figure 1.
Figure 4 is an end elevation of the classifier..
The improved classifier comprises a boxlike tank 1 of appropriate area divided. transversely by a partition 2, hereinafter termed the floor, which is inclined downwardly in the direction of feed of the material, the tank below the partition being a series of separating or classifyingchambers 8, 9, 10 and 11 by partitions 12. These partitions extend to and are secured to the side walls of the tank but terminate above the floor, leaving communicating passages 13 between the respective chambers. A sup ply pipe 14 leads beneath the tank and has outlets 15, 16, 17 and 18 communicating With the respective chambers 3, 4, 5 and 6, each outlet being controlled by a valve 19. The floor is perforated at 20 to permit the water rising in the chambers below the floor to geach the classifying chambers above the oor.
The classifying chamber 8 is the initial receiving chamber and arranged on one side of the tank at the upper end is a feeder 21 into which material to be classified is placed,
this feeder communicating at its lower end, as at 22, with theclassifying chamber 8. In the side wall opposite the feeder 21 each classifying chamber is provided with a launder indicated at 23, and the sidewall defining the particular classifying chamber is of re duced height to permit the overflow to reach the launder. Preferably, the side walls of the respective classifying chambers terminate at successively increasing heights in the direction of feed of the material, as indicated at 24 in Figure 3.
A receiver 25 is secured to the end wall of the tank beyond the final classifying chamber 11 and formed with a discharge 26 for the delivery of the material. The end Wall of the tank between the final chamber 11 and the receiver 25 is of reduced height to provide a passage 27 in which the material from the final chamber can reach the receiver.
In operating the device, coal or such other ore as may be used in delivered into the feeder 21 and gravitates into the initial classifying chamber 8, finally resting upon the perforated bottom 2 of that chamber. The valves 19 controlling the outlets 15, 16, 17 and 18 have been opened to a degree to permit currents of Water of increasing intensity to flow through the respective chambers 3, 4, 5 and 6. The water rising through the perforated floor of the initial classifying chamber 8 separates such lighter particles ticular force, and de 'vers the same to the launder 23 connected with that chamber.
The heavier particles gravitate.along the floor to the next classifying chamber where the are met by a heavier current of water an particles of reater weight than those separated in cham er 8, are lifted to the cooperating launder. This operation continues, the mass being caused to travel along the floor and intercepted in each classifying chamber with water currents of increasing strength to continue separation of relatively heavier particles during the separating proo ess. In the final classifyin chamber, the current is suflicient to lift al of the particles of material therein and deliver the same to the receiver for conveyance to any desired point.
Obviously, the pressure of water in each of the classifying chambers may be adjusted by manipulation of the respective valvesto gain that force required for the particular separation. 1
The number and size of the perforations 20in the floor are determined by the well established principles of hydraulics. The volume of water required to' maintain in a condition of teeter, the material in any given compartment may be determined by experiment. I
As the most desirable, effective head of water has been determined to be about 0.5 foot, the total area of the orifices under any given subchaniber, is calculated to deliver the required quantity'of water under that head, and the size and number of orifices selected to suit the convenience of the operator, uniformly spaced apart in the screen. If the apparatus be large, it is preferred to graduate the size of orifices to compensate for the greater head toward the left half of any subchamber, as viewed in Figure 2.
The different products and water are discharged into dewatering boxes in any approved manner, the excess of water overflowing the upper edge of the dewatering boxes. Excess water above that required for the subsequent disposition of the products of the apparatus may be removed in dewatering boxes, dewatering elevators or any other suitable apparatus common to the industry.
What I claim to be new is:
In a classifier, the combination of a fixed container, a perforated partition arranged transversely and obliquely of the container and which divides the container into an upper and lower chamber, 'a pluralit of vertically arranged partitions WhlCh dlVldG the uppermost part .of the container into a plurality of upper sub-chambers, each subchamber being comparatively long transversely of the container and comparatively short longitudinally thereof, means for feeding the material to the first sub-chamber at one end thereof adjacent a corner of the container, the said vertical partitions being spaced away from the perforated partition, thus leaving a transverse sub-chamber having an oblique floor, the end wall of the container forming one wall of the last vertical chamber terminating short of the top edge of said container to form an overflow passage for the material, a separate receiving chamber with which the overflow passage connects, a side refuse chamber communicating with each vertical chamber at different distances from the top of the container, an additional group of vertically arranged partitions beneath the transverse partition which divide the lowermost part of the container into a plurality of lower sub-chambers, and which partitions extend upwardly from the floor of the container to and against the transverse partition, means for supplying water under constant pressure and a valve for each lower sub chamber whereby streams of water of varying intensity are conducted ,into the lower sub-chambers.
In testimony whereof I aflix my signature.
' BYRON M. BIB-D.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US170977A US1715693A (en) | 1927-02-25 | 1927-02-25 | Ore classifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US170977A US1715693A (en) | 1927-02-25 | 1927-02-25 | Ore classifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1715693A true US1715693A (en) | 1929-06-04 |
Family
ID=22622042
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US170977A Expired - Lifetime US1715693A (en) | 1927-02-25 | 1927-02-25 | Ore classifier |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1715693A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2420180A (en) * | 1943-09-14 | 1947-05-06 | William C Laughlin | Apparatus and method for hydraulic concentration |
| US2760634A (en) * | 1951-12-18 | 1956-08-28 | Conveyor Company Inc | Method and apparatus for hydraulic classification involving settling |
| US3261559A (en) * | 1961-08-07 | 1966-07-19 | Consolidation Coal Co | Gravity separation of coal ore |
| US4022685A (en) * | 1974-06-28 | 1977-05-10 | Michel Tisseau | Method of separating products of different density and apparatus for carrying out the method |
-
1927
- 1927-02-25 US US170977A patent/US1715693A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2420180A (en) * | 1943-09-14 | 1947-05-06 | William C Laughlin | Apparatus and method for hydraulic concentration |
| US2760634A (en) * | 1951-12-18 | 1956-08-28 | Conveyor Company Inc | Method and apparatus for hydraulic classification involving settling |
| US3261559A (en) * | 1961-08-07 | 1966-07-19 | Consolidation Coal Co | Gravity separation of coal ore |
| US4022685A (en) * | 1974-06-28 | 1977-05-10 | Michel Tisseau | Method of separating products of different density and apparatus for carrying out the method |
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