US447027A - Ore-separating apparatus - Google Patents
Ore-separating apparatus Download PDFInfo
- Publication number
- US447027A US447027A US447027DA US447027A US 447027 A US447027 A US 447027A US 447027D A US447027D A US 447027DA US 447027 A US447027 A US 447027A
- Authority
- US
- United States
- Prior art keywords
- ore
- receptacle
- separating apparatus
- air
- receptacles
- 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
- 239000000463 material Substances 0.000 description 16
- 239000002245 particle Substances 0.000 description 10
- 238000000926 separation method Methods 0.000 description 10
- 230000005484 gravity Effects 0.000 description 8
- 241000054817 Lycaena dione Species 0.000 description 6
- 229910052500 inorganic mineral Inorganic materials 0.000 description 6
- 239000011707 mineral Substances 0.000 description 6
- 229910052683 pyrite Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 229910052949 galena Inorganic materials 0.000 description 4
- WGPCGCOKHWGKJJ-UHFFFAOYSA-N sulfanylidenezinc Chemical compound [Zn]=S WGPCGCOKHWGKJJ-UHFFFAOYSA-N 0.000 description 4
- UCKMPCXJQFINFW-UHFFFAOYSA-N sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 4
- 229910052984 zinc sulfide Inorganic materials 0.000 description 4
- 230000001174 ascending Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 229910052904 quartz Inorganic materials 0.000 description 2
- 230000000630 rising Effects 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
Definitions
- My invention relates, more particularly stated,to animprovement for use in the known manner of ore separation, wherein to attain the desired result the ore in a pulverized condition is forced by means of air-currents over a series of receptacles located below the plane of the air-currents and into which the particles of ore carried by the air-currents are dropped successively by and according to their specific gravities.
- the object of my improvement is to enable the manner stated as having been hitherto employed for producing the separation to be the more effectually practiced, and this I accomplish by my improved apparatus hereinafter described, and shown in sectional elevation in the acc mpanying drawing.
- A denotes a building or inclosure containing the entire mechanism-namely, a pulverizing-maohine Bin which 1) denotes heaters and situated atthe lower end of an inclined course of the material acted upon and which is defined by the inlet ends of any desired number of vertically-disposed receptacles or bins, of which five are shown and indicated, respectively, by f, g, h, 2 andj, and an exhaust-fan O at the opposite upper end of the inclined plane, the exhaust-fan being provided with an inlet-pipe d.
- the bins are provided, as shown, with hopper-shaped bottoms having the outlets 0.
- the first or lowest receptacle f is a false bottom Z, inclining downward to coincide with the upper part of the base of a return-passage m, leading to an upper airinlet passage 0 in the pulverizing-machine, and a valve n is provided at the inlet end of the passage m.
- the pulverizing-machine B is partitioned off, as shown, from the compartment containing the bins and communicates therewith above the latter through an opening covered by a screen 19.
- the partitions 10 between and forming the receptacles extend from the fiooro' and increase in height from that nearest the screen 19 to the end of the compartment containing the receptacles,
- the exhaust-fan C communicates with it, and operates when set in motion to draw air-currents upward through the compartment from the pulverizer in a direction inclined from the horizontal, the base of the air-currents being about at the line indicated by the arrows at e.
- the ore as it is pulverized is drawn by the suction effect of the fan 0 with the air-currents through the screen 19 in the'ascending direction indicated by the arrows 6.
- the heaviest particles of the ore drop into the receptacle f, the next heaviest into the receptacle g, and so on, the particles dropping into the successive receptacles in the order of their specific gravities, the different lots or grades being prevented from becoming intermixed in the receptacles by the successively rising partitions, which, as indicated by the curved arrows at k, intercept the material belonging in the bins they respectively define against being passed by its inertia beyond the bin in which it belongs. In many cases a portion of the ore will not be pulverized sufficiently to have effected an approxi* mately complete separation of mineral or metal from the inclosing rock or gangue.
- the largest percentage of galena would be found in the receptacle g, of the iron pyr ite in the receptacle h, the greatest value in gray copper in the receptacle i, and a mingled material composed of zinc-blende and gray copper With some of the finer particles of galena and iron pyrite in the receptacle 3'.
- Each receptacle would then contain the pulverized mineral separated for the most part in a degree, each variety being largely by itself, but all mingled With larger particles of gangue of a degree of specific gravity relative to each separation; and as thus reduced the material is in condition to be further treated, for sizing it or screening it, if necessary, and to have the largest percentage of each variety of mineral value kept by itself.
- An ore-separating apparatus comprising, in combination with an inclosure A, a pulverizer 13, having an air-inlet passage 0 and communicating through an opening covered by a screen 1) with a compartment containing receptacles having their defining partitions extended successively higher from the pulverizer to define a gradually-rising plane, an exhaust-fan C, communicating with the said compartment near the upper end of the inclined plane, a false bottom Z in the lowermost receptacle, a return-passage m, leading in to the p ulverizer through its air-inlet c, and a valve 12 for the passage m, substantially as and for the purpose set forth.
Description
(No Model.) A
J.- K. HALLOWELL.
ORE SEPARATI NG APPARATUS. I No. 447,027. I PatentedIF-eo. 24, 1891.
as co., mow-mum, WASHINGKON, n. c.
UNITED STATES PATENT Unmet,
JOllN K. HALLOVEEL, OF CAMDEN, NE\V JERSEY.
ORE-SEPARATING APPARATUS.
SPECIFICATION forming part Of Letters Patent N0. 447,027, dated February 24, 1891. Application filed June 13, 1888- Serial No. 277,023. (No model.)
To all whom it may concern.-
Be it known that I, J OHN K. HALLOWELL, of Camden, in the county of Camden and State of New Jersey, have invented certain new and useful Improvements in Ore-Separating Apparatus, of which the following is a specification.
My invention relates, more particularly stated,to animprovement for use in the known manner of ore separation, wherein to attain the desired result the ore in a pulverized condition is forced by means of air-currents over a series of receptacles located below the plane of the air-currents and into which the particles of ore carried by the air-currents are dropped successively by and according to their specific gravities. 1
The object of my improvement is to enable the manner stated as having been hitherto employed for producing the separation to be the more effectually practiced, and this I accomplish by my improved apparatus hereinafter described, and shown in sectional elevation in the acc mpanying drawing. I
' A denotes a building or inclosure containing the entire mechanism-namely, a pulverizing-maohine Bin which 1) denotes heaters and situated atthe lower end of an inclined course of the material acted upon and which is defined by the inlet ends of any desired number of vertically-disposed receptacles or bins, of which five are shown and indicated, respectively, by f, g, h, 2 andj, and an exhaust-fan O at the opposite upper end of the inclined plane, the exhaust-fan being provided with an inlet-pipe d. The bins are provided, as shown, with hopper-shaped bottoms having the outlets 0. In the first or lowest receptacle f is a false bottom Z, inclining downward to coincide with the upper part of the base of a return-passage m, leading to an upper airinlet passage 0 in the pulverizing-machine, and a valve n is provided at the inlet end of the passage m. The pulverizing-machine B is partitioned off, as shown, from the compartment containing the bins and communicates therewith above the latter through an opening covered by a screen 19. The partitions 10 between and forming the receptacles extend from the fiooro' and increase in height from that nearest the screen 19 to the end of the compartment containing the receptacles,
where the exhaust-fan C communicates with it, and operates when set in motion to draw air-currents upward through the compartment from the pulverizer in a direction inclined from the horizontal, the base of the air-currents being about at the line indicated by the arrows at e. The ore as it is pulverized is drawn by the suction effect of the fan 0 with the air-currents through the screen 19 in the'ascending direction indicated by the arrows 6. The heaviest particles of the ore drop into the receptacle f, the next heaviest into the receptacle g, and so on, the particles dropping into the successive receptacles in the order of their specific gravities, the different lots or grades being prevented from becoming intermixed in the receptacles by the successively rising partitions, which, as indicated by the curved arrows at k, intercept the material belonging in the bins they respectively define against being passed by its inertia beyond the bin in which it belongs. In many cases a portion of the ore will not be pulverized sufficiently to have effected an approxi* mately complete separation of mineral or metal from the inclosing rock or gangue. This portion will seek the bin f, lodging on the false bottom Z thereof and passing thence through the air-inlet 0 back into the pulverizer to be again subjected to its action. Where repulverizing of the material is not required, the valve n, otherwise open, is closed and the false bottom 1 removed to permit, as in the case of all the receptacles, the material to lodge in thehopper-bottoms of thebins,whence it may be withdrawn through the outlets 0. This manner of effecting the separation according to differences in the specific gravity of the material isadvantageo'us both in complex sulphide and tellnride ores, wherein the ICO To definitely describe the effect of the treatment with my improved apparatus upon a particular kind of ore, take a complex sulphide ore, the value of which is in silver, but the material of Which is composed of quartz, galena, iron pyrite, gray copper, and zincblende. By the action .of the described apparatus the largest percentage of galenawould be found in the receptacle g, of the iron pyr ite in the receptacle h, the greatest value in gray copper in the receptacle i, and a mingled material composed of zinc-blende and gray copper With some of the finer particles of galena and iron pyrite in the receptacle 3'. Each receptacle would then contain the pulverized mineral separated for the most part in a degree, each variety being largely by itself, but all mingled With larger particles of gangue of a degree of specific gravity relative to each separation; and as thus reduced the material is in condition to be further treated, for sizing it or screening it, if necessary, and to have the largest percentage of each variety of mineral value kept by itself.
That I claim as new, and desire to secure by Letters Patent, is
An ore-separating apparatus comprising, in combination with an inclosure A, a pulverizer 13, having an air-inlet passage 0 and communicating through an opening covered by a screen 1) with a compartment containing receptacles having their defining partitions extended successively higher from the pulverizer to define a gradually-rising plane, an exhaust-fan C, communicating with the said compartment near the upper end of the inclined plane, a false bottom Z in the lowermost receptacle, a return-passage m, leading in to the p ulverizer through its air-inlet c, and a valve 12 for the passage m, substantially as and for the purpose set forth.
JOHN K. IIALLO\VELL.
Witnesses:
F. G. FAROR, CHAS. W. PILE.
Publications (1)
Publication Number | Publication Date |
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US447027A true US447027A (en) | 1891-02-24 |
Family
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Family Applications (1)
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US447027D Expired - Lifetime US447027A (en) | Ore-separating apparatus |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3062458A (en) * | 1957-09-09 | 1962-11-06 | Arthur G Dearing | Ore upgrader |
US3929293A (en) * | 1973-05-16 | 1975-12-30 | Pennsylvania Crusher Corp | Shredder crusher material reducer |
US3933626A (en) * | 1973-07-12 | 1976-01-20 | Ottawa Silica Company | Classifier for particulate material |
US4304661A (en) * | 1980-03-10 | 1981-12-08 | Nelson George S | Machines for concentrating ore |
US20020175113A1 (en) * | 1998-05-22 | 2002-11-28 | Hannu Tahkanen | Method and apparatus for sorting of chips |
-
0
- US US447027D patent/US447027A/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3062458A (en) * | 1957-09-09 | 1962-11-06 | Arthur G Dearing | Ore upgrader |
US3929293A (en) * | 1973-05-16 | 1975-12-30 | Pennsylvania Crusher Corp | Shredder crusher material reducer |
US3933626A (en) * | 1973-07-12 | 1976-01-20 | Ottawa Silica Company | Classifier for particulate material |
US4304661A (en) * | 1980-03-10 | 1981-12-08 | Nelson George S | Machines for concentrating ore |
US20020175113A1 (en) * | 1998-05-22 | 2002-11-28 | Hannu Tahkanen | Method and apparatus for sorting of chips |
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