US1987221A - Process of treating micaceous ores - Google Patents
Process of treating micaceous ores Download PDFInfo
- Publication number
- US1987221A US1987221A US678316A US67831633A US1987221A US 1987221 A US1987221 A US 1987221A US 678316 A US678316 A US 678316A US 67831633 A US67831633 A US 67831633A US 1987221 A US1987221 A US 1987221A
- Authority
- US
- United States
- Prior art keywords
- ore
- micaceous
- gangue
- mica
- ores
- 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
- 238000000034 method Methods 0.000 title description 20
- 239000010445 mica Substances 0.000 description 18
- 229910052618 mica group Inorganic materials 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- NLKNQRATVPKPDG-UHFFFAOYSA-M potassium iodide Chemical compound [K+].[I-] NLKNQRATVPKPDG-UHFFFAOYSA-M 0.000 description 9
- 239000002253 acid Substances 0.000 description 7
- 238000000227 grinding Methods 0.000 description 7
- 238000004299 exfoliation Methods 0.000 description 6
- 239000010455 vermiculite Substances 0.000 description 6
- 229910052902 vermiculite Inorganic materials 0.000 description 6
- 235000019354 vermiculite Nutrition 0.000 description 6
- 238000004040 coloring Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 229910000906 Bronze Inorganic materials 0.000 description 3
- 239000010974 bronze Substances 0.000 description 3
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- VBIXEXWLHSRNKB-UHFFFAOYSA-N ammonium oxalate Chemical compound [NH4+].[NH4+].[O-]C(=O)C([O-])=O VBIXEXWLHSRNKB-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000009533 lab test Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000001238 wet grinding Methods 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241001272996 Polyphylla fullo Species 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
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
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S106/00—Compositions: coating or plastic
- Y10S106/03—Mica
Definitions
- This invention relates to the treatment 'of micaceous ores and particularly to ores of the character of vermiculite.
- the general object of this invention is to provide a process of cleaning, coloring and improving exfoliation of crude micaceous ores and a further object is to provide means whereby the fine mica flakes or particles may be given either a light golden color, a light bronze color or a gray 10 or silvery color while the mica is being liberated from the gangue and exfoliated.
- the vermiculite or crude ore is wet ground, that is, the crude ore is washed and ground in a grinding mill with water.
- a grinding mill consisting of a large circular pan with steel mullers running in a circular path in the pan. Such a mill as this rubs all the surfaces of the vermiculite clean.
- the ore is ground to a fineness depending upon the laboratory tests of the ore, certain ore requiring grinding of thirty mesh while other ore may require grinding to forty mesh to finally effect perfect liberation of the mica from the gangue and foreign minerals.
- This wet grinding process partially eliminates the gangue as well as the foreign matter.
- the Whole mass of gangue and vermiculite is now in a powdered form.
- the partially liberated vermiculite is now placed in a tank which is preferably in the form of a long sloping tank 16 feet in length, four feet wide and four feet deep at the lower or has two screw conveyors installed therein and extending longitudinally of the tank.
- a tank which is preferably in the form of a long sloping tank 16 feet in length, four feet wide and four feet deep at the lower or has two screw conveyors installed therein and extending longitudinally of the tank.
- an acid solution such as hereafter stated and the ore is placed within the receiving end of the tank.
- the ore remains in the acid solution for a period of a few moments up to twenty+four hours depending upon the character of the ore which is shown by laboratory tests and during this period the mica is given the color desired while at the same receiving end of the tank.
- This tank preferably time, the acidified solution secures complete liberation of the gangue from the mica.
- a solution of potassium iodide and sodium I sulphate gives a light golden color to the mica.
- Potassium iodide alone gives a light bronze color
- Ammonium oxalate gives a gray color, but neither sulphuric acid or hydrochloric acid colors the mica but merely leaves it with its natural silvery 10 color to the mica.
- the screw conveyors are put into motion and the mica together with the gangue are 15 carried upward over the sloping bottom of the tank out of the acidified solution.
- the last step of the process consists of mechanically separating the mica from the gangue by means of jigs, classifiers or/and concentrating tables of com- 20 mon and ordinary construction. At the same time plenty of wash water is used to remove all acids.
- the finished product is mica in Enhance velvet-like condition and colored according to the colors above stated.
- the vermiculite is ground with water to the desired fineness, the water is decanted, as previously stated, leaving about twenty per cent of 80 moisture in the ground ore.
- the ground ore is' then passed to mechanical separating means, such as jigs, classifiers, and ore concentrator tables so as to separate the mica from the gangue.
- the separated mica is then passed into the coloring 35 tank, as before described, which contains an acidified solution, as before stated, and after remaining in the coloring tank and under the action of the acidified solution for a predeterminedperiod, as before stated, the ore is removed from 40 the tank and washed to remove all chemical residue.
- the mica which is the product of my process has many uses. Thus it may be used in wall tinting, on wall paper, for the formation of gilt, bronze, grey and silver paints, for the formation of insulating boards and panels. .These are only a few of the uses for which my product is adapted.
- a process of treating micaceous ores which consists in wet grinding the ores to a predetermined degree of fineness, removing a predetermined amount of water from the ground ore to leave approximately twenty per cent of moisture in the ore, submitting the ore to the action of an acid solution of predetermined strength for from a period of a few minutes to twenty-four hours, the solution being of such strength as ,to accomplish the complete liberation of the gangue from the mica without affecting exfoliation, then mechanically separating the micaceous portion of the ore from the gangue.
- a process of treating micaceous ores which includes the following stepsz-water grinding the ore to a predetermined degree of fineness, removing excess water from the ore to a degree having about 20% of the water in the ground mass, subjecting the micaceous portion of the ore to the action of a solution of ammonium oxalate, mechanically'separating the micaceous portion of the ore from the gangue, and washing the micaceous portion of the ore to remove the acid.
- a process of treating micaceous ores which consists in grinding the ore with water to a predetermined degree of fineness, decanting the water from the ore to a degree leaving about twenty per cent of water in the ground mass, mechanically separating the micaceous portion of the ore from the gangue, submitting the micaceous portion of the ore with whatever gangue may still remain with the micaceous portion to the action of an acidified solution of a strength not greater than will completely liberate the gangue from the mica without affecting exfoliation to thereby further separate the micaceous portion of the ore from the gangue and at the same time color the micaceous portion of the ore, and washing the micaceous portion of the ore to remove all chemical residue.
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
Description
Patented Jan. 8, 1935 UNITED STATES PATENT OFFIC No Drawing.
Application June 29, 1933,
Serial No. 678,316 '4 Claims. (01. 252-8) This invention relates to the treatment 'of micaceous ores and particularly to ores of the character of vermiculite.
The general object of this invention is to provide a process of cleaning, coloring and improving exfoliation of crude micaceous ores and a further object is to provide means whereby the fine mica flakes or particles may be given either a light golden color, a light bronze color or a gray 10 or silvery color while the mica is being liberated from the gangue and exfoliated.
In accordance with my process, the vermiculite or crude ore is wet ground, that is, the crude ore is washed and ground in a grinding mill with water. Preferably I use a grinding mill consisting of a large circular pan with steel mullers running in a circular path in the pan. Such a mill as this rubs all the surfaces of the vermiculite clean. The ore is ground to a fineness depending upon the laboratory tests of the ore, certain ore requiring grinding of thirty mesh while other ore may require grinding to forty mesh to finally effect perfect liberation of the mica from the gangue and foreign minerals. This wet grinding process partially eliminates the gangue as well as the foreign matter. The Whole mass of gangue and vermiculite is now in a powdered form. The water is now decanted from the ore so that only about twenty per cent of moisture remains in the ore. This is the natural amount of moisture absorbed by the ore. Care should be taken to avoid excessive decantation or dehydration to an extent which would remove natural moisture. By leaving approximately twenty per cent of moisture in the ground ore, exfoliation I find is very greatly improved whereas if the ore is entirely de-hydrated, exfoliation is checked and the resulting product is much less valuable than where dehydration has been 40 checked at the point indicated.
The partially liberated vermiculite is now placed in a tank which is preferably in the form of a long sloping tank 16 feet in length, four feet wide and four feet deep at the lower or has two screw conveyors installed therein and extending longitudinally of the tank. In the lower end of the tank is placed an acid solution such as hereafter stated and the ore is placed within the receiving end of the tank. The ore remains in the acid solution for a period of a few moments up to twenty+four hours depending upon the character of the ore which is shown by laboratory tests and during this period the mica is given the color desired while at the same receiving end of the tank. This tank preferably time, the acidified solution secures complete liberation of the gangue from the mica.
The following acids are used for fully liberating the gangue and coloring the mica. f
A solution of potassium iodide and sodium I sulphate gives a light golden color to the mica. Potassium iodide alone gives a light bronze color, Ammonium oxalate gives a gray color, but neither sulphuric acid or hydrochloric acid colors the mica but merely leaves it with its natural silvery 10 color to the mica.
After the mass has remained in this solution for a period of from a few moments to twentyfour hours, the screw conveyors are put into motion and the mica together with the gangue are 15 carried upward over the sloping bottom of the tank out of the acidified solution. The last step of the process consists of mechanically separating the mica from the gangue by means of jigs, classifiers or/and concentrating tables of com- 20 mon and ordinary construction. At the same time plenty of wash water is used to remove all acids. The finished product is mica in afine velvet-like condition and colored according to the colors above stated.
An alternative process to that above described is as follows:
The vermiculite is ground with water to the desired fineness, the water is decanted, as previously stated, leaving about twenty per cent of 80 moisture in the ground ore. The ground ore is' then passed to mechanical separating means, such as jigs, classifiers, and ore concentrator tables so as to separate the mica from the gangue. The separated mica is then passed into the coloring 35 tank, as before described, which contains an acidified solution, as before stated, and after remaining in the coloring tank and under the action of the acidified solution for a predeterminedperiod, as before stated, the ore is removed from 40 the tank and washed to remove all chemical residue.
In the first stated process, the operation of washing and mechanical separation is combined in a singlestep and constitutes the the process. In other words, there are three steps in the process first described andfour steps in Q the process as last described. The process produces a very finely ground, velvety product having the coloration stated and 50 this product is capable of a large variety of uses. To my knowledge, thousands of dollars have been spent in searching for the process for preparing a product of this character from crude micaceous ores but no method known to me secures the result last step of 45:"
- about 20% micaceous portion of the ore to the action of a of my method. By this method or process, I separate the micaceous material from the gangue, improve exfoliation and at the same time color the small flakes or particles of mica.
The mica which is the product of my process has many uses. Thus it may be used in wall tinting, on wall paper, for the formation of gilt, bronze, grey and silver paints, for the formation of insulating boards and panels. .These are only a few of the uses for which my product is adapted.
I claim:-
1. A process of treating micaceous ores which consists in wet grinding the ores to a predetermined degree of fineness, removing a predetermined amount of water from the ground ore to leave approximately twenty per cent of moisture in the ore, submitting the ore to the action of an acid solution of predetermined strength for from a period of a few minutes to twenty-four hours, the solution being of such strength as ,to accomplish the complete liberation of the gangue from the mica without affecting exfoliation, then mechanically separating the micaceous portion of the ore from the gangue.
2.'A process of treating micaceous ores which includes the following steps:-w'ater grinding the ore to a predetermined degree of fineness, removing excess water from the ore to a degree having of water in the mass, subjecting the solution of potassium iodide and sodium sulphite,
mechanically separating the micaceous portion of the ore from the gangue, and washing the micaceous portion of the ore to remove the acid.
3. A process of treating micaceous ores which includes the following stepsz-water grinding the ore to a predetermined degree of fineness, removing excess water from the ore to a degree having about 20% of the water in the ground mass, subjecting the micaceous portion of the ore to the action of a solution of ammonium oxalate, mechanically'separating the micaceous portion of the ore from the gangue, and washing the micaceous portion of the ore to remove the acid.
4. A process of treating micaceous ores which consists in grinding the ore with water to a predetermined degree of fineness, decanting the water from the ore to a degree leaving about twenty per cent of water in the ground mass, mechanically separating the micaceous portion of the ore from the gangue, submitting the micaceous portion of the ore with whatever gangue may still remain with the micaceous portion to the action of an acidified solution of a strength not greater than will completely liberate the gangue from the mica without affecting exfoliation to thereby further separate the micaceous portion of the ore from the gangue and at the same time color the micaceous portion of the ore, and washing the micaceous portion of the ore to remove all chemical residue.
JULIUS T. STROEHLKE.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US678316A US1987221A (en) | 1933-06-29 | 1933-06-29 | Process of treating micaceous ores |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US678316A US1987221A (en) | 1933-06-29 | 1933-06-29 | Process of treating micaceous ores |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1987221A true US1987221A (en) | 1935-01-08 |
Family
ID=24722307
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US678316A Expired - Lifetime US1987221A (en) | 1933-06-29 | 1933-06-29 | Process of treating micaceous ores |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1987221A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2492208A (en) * | 1945-04-16 | 1949-12-27 | Joseph B Barnes | Process of exfoliating and bleaching vermiculite |
| US2510971A (en) * | 1944-08-31 | 1950-06-13 | Harvie W Goddin | Pyroxite compositions |
| US3076546A (en) * | 1959-04-20 | 1963-02-05 | Zonolite Company | Vermiculite concentration |
| US4400297A (en) * | 1980-10-14 | 1983-08-23 | Morca, Inc. | Modified hydrated magnesium aluminosilicates and method of preparation |
| US4515633A (en) * | 1980-10-14 | 1985-05-07 | Morca, Inc. | Polymeric materials combined with modified hydrated magnesium aluminosilicates |
| US20060160940A1 (en) * | 2003-03-03 | 2006-07-20 | Andreas Muhlebach | Process for intercalating natural or szynthetic clays with block or comb copolymers |
-
1933
- 1933-06-29 US US678316A patent/US1987221A/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2510971A (en) * | 1944-08-31 | 1950-06-13 | Harvie W Goddin | Pyroxite compositions |
| US2492208A (en) * | 1945-04-16 | 1949-12-27 | Joseph B Barnes | Process of exfoliating and bleaching vermiculite |
| US3076546A (en) * | 1959-04-20 | 1963-02-05 | Zonolite Company | Vermiculite concentration |
| US4400297A (en) * | 1980-10-14 | 1983-08-23 | Morca, Inc. | Modified hydrated magnesium aluminosilicates and method of preparation |
| US4515633A (en) * | 1980-10-14 | 1985-05-07 | Morca, Inc. | Polymeric materials combined with modified hydrated magnesium aluminosilicates |
| US20060160940A1 (en) * | 2003-03-03 | 2006-07-20 | Andreas Muhlebach | Process for intercalating natural or szynthetic clays with block or comb copolymers |
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