US504201A - Art of concentrating magnetic iron ore - Google Patents
Art of concentrating magnetic iron ore Download PDFInfo
- Publication number
- US504201A US504201A US504201DA US504201A US 504201 A US504201 A US 504201A US 504201D A US504201D A US 504201DA US 504201 A US504201 A US 504201A
- Authority
- US
- United States
- Prior art keywords
- ore
- mass
- magnets
- iron ore
- magnetic iron
- 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.)
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title description 56
- 229910052742 iron Inorganic materials 0.000 title description 28
- 239000012141 concentrate Substances 0.000 description 20
- 239000002245 particle Substances 0.000 description 18
- 238000001035 drying Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 239000006249 magnetic particle Substances 0.000 description 4
- 239000006148 magnetic separator Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000010878 waste rock Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
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
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/10—Magnetic separation acting directly on the substance being separated with cylindrical material carriers
- B03C1/14—Magnetic separation acting directly on the substance being separated with cylindrical material carriers with non-movable magnets
Definitions
- WITNESSES v YINVENTOR' ATTORNEYS.
- the object of this invention is an improvement in the art of concentrating magnetic iron ore whereby a concentrate is obtained which is practically free from phosphorus or other impurities, the presence of which when exceeding one tenth of one per cent. would render the concentrate unfit for the manufacture of steel.
- FIG. 1 is a longitudinal vertical section of a magnetic separator to be used when the comminuted ore is in a wet state.
- Fig. 2 is a plan or top view of a magnetic separator which may be used when the comminuted ore is in a dry state.
- Fig. 3 is a side elevation of an ore roasting furnace which can be used in carrying outone step of my new process.
- the object of my invention is to reduce the expense in labor and fuel to such an extent that not only mines yielding low grade ores can be worked with profit but also very high grade ores can be treated with the least possible expense so as to yield a concentrate practically free from gangue.
- I proceed as follows: I first crush the ore in the wet state to a fineness of from one-fourth to one-sixteenth of an inch according to the natural granular formation'of the ore to be treated and then expose the coarsely crushed mass, while in a wet state, to the action of magnets.
- Fig. 1 of the drawings in which the letterA designates an endless belt which extends over rollers B B and is placed in an inclined position.
- F is a magnet which issituated in the interior of the belt A close to its upper branch.
- vE is a trough over which the crushed ore mixed with water is fed to the belt A and S is a spray pipe for washing the particles of ore which are attracted by the magnet.
- the belt moves in the direction of arrowl and the particles which are attracted by the magnet are carried by the belt over the pulley B and they are collected in the receiver L.
- the particles which are not attracted by the magnet run down over the pulley B and are collected in the receiver K.
- the mass which has been collected in the receiverL is composed of particles from a quarter-of an inch down and many of the particles are composed of iron ore and gangue still attached or adhering to the same and in order to eliminate this gangue from the mass I submitthe same while wet to a second crushing operation reducing the particles into a, very fine state and then I dry the mass by preference under constant agitation so as to detach the particles of gangue which adhere to the particles of iron ore as long asthey are moist.
- I can use an ordinary ore roasting furnace of well known construction such as illustrated in Fig. 3. After the mass has. been thoroughly dried, I expose the same to the action I seen, that my new process consists essentially of magnets.
- a machine such as shown in Fig. 2 of the drawings.
- a main belt A and a secondary belt B which extends at right angles over the main belt A and in the interior of which close-toitslowerbranch are situated the magnets F.
- the mass to be separated is fed to the main belt A through a hopper E and the magnetic particles which are attracted by the magnets F, are carried away by the belt Bin thed-irection of arrow 1 while the gangue which remains on the belt A is carried away inthe direction of arrow 2.
Description
(No Model.) I
G. OONKLING. ART OF GONUENTRATING MAGNETIU IRON-ORE."
N'o. 504,201. Patented Aug. 29, 11-893.
WITNESSES: v YINVENTOR' ATTORNEYS.
UNITED STATES PATENT OFFICE.
GURDON OONKLING, OF GLENS FALLS, NEW YORK.
ART OF CONCENTRATING MAGNETIC IRON ORE.
SPECIFICATION forming part of Letters Patent No. 504,201, dated August 29, 1893.
Application filed January 16,1893. Serial No. 45 8,546. (No model.)
To all whom it may concern:
Be it known that I, GURDON CONKLING, a citizen of the United States, residing at Glens Falls, in the county of Warren and State of New York, have invented new and useful Improvements in the Art of Concentrating Magnetic Iron Ore, of which the following is a specification.
The object of this invention is an improvement in the art of concentrating magnetic iron ore whereby a concentrate is obtained which is practically free from phosphorus or other impurities, the presence of which when exceeding one tenth of one per cent. would render the concentrate unfit for the manufacture of steel.
The apparatus which may be used in carrying out my invention, is illustrated in the accompanying drawings in which-- Figure 1,represents a longitudinal vertical section of a magnetic separator to be used when the comminuted ore is in a wet state. Fig. 2, is a plan or top view of a magnetic separator which may be used when the comminuted ore is in a dry state. Fig. 3 is a side elevation of an ore roasting furnace which can be used in carrying outone step of my new process.
After a very large number of experiments in concentrating iron ore which I have carried on during the last fifteen years, I have found-that in order to obtain a high grade concentrate containing from sixty to seventytwo per cent. of metallic iron, it is necessary to crush the ore into a very fine state and then to expose the same to the action of magnets in a perfectly dry state. If the finely crushed mass is exposed to the action of magnets in a wet state, fine particles of gangue adhere to the iron particles which are attracted by the magnets and in the majority of cases the concentrate is rendered unfit for the manufacture of steel. I have also found that the entire bulk of the ore coming either out of the mines or from the dump or waste piles, contains from two to ten per cent. of moisture varying at times largely from atmospheric causes. To be concentrated under the ordinary process of dry concentration the usual course is either to crush the mass to the re quired fineness in a wet state and then to dry the finely crushed mass and expose it to the action of magnets or the raw mass is dried first, then crushed to the required fineness and finally exposed to the action of magnets. In either case the entire bulk of the mass under treatment has to be dried which involves considerable expense in labor and fuel. In treating low grade ores this expense in many cases is so great that it exceeds the profit de rived from the concentrate and many mines have been left idle on account of the great expense involved in concentrating the ore.
The object of my invention is to reduce the expense in labor and fuel to such an extent that not only mines yielding low grade ores can be worked with profit but also very high grade ores can be treated with the least possible expense so as to yield a concentrate practically free from gangue. For this purpose I proceed as follows: I first crush the ore in the wet state to a fineness of from one-fourth to one-sixteenth of an inch according to the natural granular formation'of the ore to be treated and then expose the coarsely crushed mass, while in a wet state, to the action of magnets.
In carrying out this process an apparatus may be used such as illustrated in Fig. 1 of the drawings in which the letterA designates an endless belt which extends over rollers B B and is placed in an inclined position.
F is a magnet which issituated in the interior of the belt A close to its upper branch.
vE is a trough over which the crushed ore mixed with water is fed to the belt A and S is a spray pipe for washing the particles of ore which are attracted by the magnet. The belt moves in the direction of arrowl and the particles which are attracted by the magnet are carried by the belt over the pulley B and they are collected in the receiver L. The particles which are not attracted by the magnet run down over the pulley B and are collected in the receiver K. The mass which has been collected in the receiverL is composed of particles from a quarter-of an inch down and many of the particles are composed of iron ore and gangue still attached or adhering to the same and in order to eliminate this gangue from the mass I submitthe same while wet to a second crushing operation reducing the particles into a, very fine state and then I dry the mass by preference under constant agitation so as to detach the particles of gangue which adhere to the particles of iron ore as long asthey are moist. For the purpose of drying the ore I can use an ordinary ore roasting furnace of well known construction such as illustrated in Fig. 3. After the mass has. been thoroughly dried, I expose the same to the action I seen, that my new process consists essentially of magnets. For this purpose I can use with advantage a machine such as shown in Fig. 2 of the drawings. a main belt A and a secondary belt B which extends at right angles over the main belt A and in the interior of which close-toitslowerbranch are situated the magnets F. The mass to be separated is fed to the main belt A through a hopper E and the magnetic particles which are attracted by the magnets F, are carried away by the belt Bin thed-irection of arrow 1 while the gangue which remains on the belt A is carried away inthe direction of arrow 2. From this description it will be seen that the crushing and recrushing of the ore is done in the wet state so that'nedustis created and the bulk of the mass to be dried is reducedto such an extent that the operation of drying can be carried out at a sufficiently low cost to render it noobstaclefrom an economicalpoint of view.
An actual test madeby me has given the following result: A mass of two thousandtwo hundred and forty pounds of lowgrade magnetic iron ore was crushed in a wet state to f consists in first coarsely crushing the orein a wet state, then exposing the crushed masswhile wet to the actionofi magnets, then rej crushing the concentrate thuso'btained while gwet, then drying the recrushed. mass and finally exposing; the dry mass to the action of magnets, substantially as'describeda one eighth of an inch, then exposed" in astream of liquid to the action of magnets withthe minimum amount of loss, say two'per cent. of magnetic particles; in the failings I found iifteen hundred and seventy pounds of'gangue or wasterock. In the mass ofisix hundred and seventy pounds saved 1 had a concentrated product of magnetic iron ore my hand in the presence of two subscribing w-itnesses-.
containing fifty per cent. of metallic" iron. The six hundred and seventy pounds thus obtained were crushed to-about one-fortieth the action of magnets as above described. The
concentrate obtained containsfrom seventy This machine consists; of.
to seventy-two per cent. of metallic iron and is practically free from gangue. In this case the bulk of the mass to be dried was reduced from two thousand two hundred and forty pounds to six hundred and seventy pounds.
From the foregoing. explanation it will be of the following steps: one, coarsely crushing theorein awetstate; two,exposing the crushed mass while wet,to the action of magnets; three, recrushin g the concentrate thus obtained,
iwh-ile wet; four, drying therecrnshed mass;
five, exposing the dry mass to the action of magnets. By these means I am enabled to obtain a concentrate of a high grade in a com paratively cheap manner. By carrying out the first operation of crushing the ore in the wet state and alsothe third operation 0t recrushi'ngthe ore in the wet state I avoid the creation of dust which is unavoidable, it the mass is crushed in a dry state. and which is injuriousto the health of the operatives and t0 the machinery, and by the secondoperation, via, exposing the crushed mass while wet, tothe actionof magnets I reduce the bulk of" the masswhich is afterward'recrushed and then dried, so that the expenseof recrushing and drying is materially reduced.
What-I claim asrnew, and desire to secure by Letters Patent, is-
The process of concentrating iron orewh-ich In testimony whereof I have hereunto set GURDON C'ON'KI'JFNG'. Witnesses:
WM. 0. HAUFF,
E. F. KASTENHUBER.
Publications (1)
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US504201A true US504201A (en) | 1893-08-29 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060081516A1 (en) * | 2004-08-13 | 2006-04-20 | Regents Of The University Of Minnesota | Fines removal apparatus and methods/systems regarding same |
US20090194470A1 (en) * | 2004-08-13 | 2009-08-06 | Hendrickson David W | Fines Removal Apparatus and Methods/Systems Regarding Same |
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0
- US US504201D patent/US504201A/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060081516A1 (en) * | 2004-08-13 | 2006-04-20 | Regents Of The University Of Minnesota | Fines removal apparatus and methods/systems regarding same |
US7347331B2 (en) | 2004-08-13 | 2008-03-25 | Regents Of The University Of Minnesota | Fines removal apparatus and methods/systems regarding same |
US20080142417A1 (en) * | 2004-08-13 | 2008-06-19 | Regents Of The University Of Minnesota | Fines removal apparatus and methods/systems regarding same |
US20090194470A1 (en) * | 2004-08-13 | 2009-08-06 | Hendrickson David W | Fines Removal Apparatus and Methods/Systems Regarding Same |
US8020706B2 (en) | 2004-08-13 | 2011-09-20 | Regents Of The University Of Minnesota | Fines removal apparatus and methods/systems regarding same |
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