US602632A - Method of obtaining free amorphous silicon - Google Patents
Method of obtaining free amorphous silicon Download PDFInfo
- Publication number
- US602632A US602632A US602632DA US602632A US 602632 A US602632 A US 602632A US 602632D A US602632D A US 602632DA US 602632 A US602632 A US 602632A
- Authority
- US
- United States
- Prior art keywords
- silicon
- sulfur
- copper
- free
- per cent
- 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
- 229910021417 amorphous silicon Inorganic materials 0.000 title description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 58
- 229910052710 silicon Inorganic materials 0.000 description 58
- 239000010703 silicon Substances 0.000 description 58
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 50
- 229910052717 sulfur Inorganic materials 0.000 description 50
- 239000011593 sulfur Substances 0.000 description 50
- 239000010949 copper Substances 0.000 description 38
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 36
- 229910052802 copper Inorganic materials 0.000 description 36
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 36
- 229910045601 alloy Inorganic materials 0.000 description 22
- 239000000956 alloy Substances 0.000 description 22
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 18
- 239000000377 silicon dioxide Substances 0.000 description 18
- KRHYYFGTRYWZRS-UHFFFAOYSA-N HF Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 10
- 150000001875 compounds Chemical class 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 239000002253 acid Substances 0.000 description 8
- 150000007513 acids Chemical class 0.000 description 8
- -1 copper-silicon Chemical compound 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 239000000843 powder Substances 0.000 description 8
- 150000004760 silicates Chemical class 0.000 description 8
- 229910000881 Cu alloy Inorganic materials 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000010298 pulverizing process Methods 0.000 description 6
- 229910000676 Si alloy Inorganic materials 0.000 description 4
- QGJOPFRUJISHPQ-UHFFFAOYSA-N carbon bisulphide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 4
- 150000001879 copper Chemical class 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- BWFPGXWASODCHM-UHFFFAOYSA-N Copper monosulfide Chemical compound [Cu]=S BWFPGXWASODCHM-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 229910052955 covellite Inorganic materials 0.000 description 2
- 229910021419 crystalline silicon Inorganic materials 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- DWFFKGPZNGKUPH-UHFFFAOYSA-N sulfanylidenesilicon Chemical compound S=[Si] DWFFKGPZNGKUPH-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/02—Silicon
- C01B33/021—Preparation
- C01B33/027—Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material
- C01B33/033—Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material by reduction of silicon halides or halosilanes with a metal or a metallic alloy as the only reducing agents
Definitions
- a copper-silicon alloy of average quality was found by chemical analysis to contain: copper, 70.05 per cent; iron, 0.87 per cent; free silicon, 19. 21 percent. combined silicon, 10.10 per cent.
- the object of my present invention is to reclaim as large a portion as possible of the 10.10 per cent. of combined silicon and convert the same into free silicon, as it is apparent that heretofore more than one-third of the total percentage of silicon in the alloy was lost in the operation.
- the alloy is finely ground and mixed with sufur, the quantity of sulfur being determined by the percentage composition of the alloy.
- This finely-ground mixture is heated in a closed vessel to a temperature which preferably ranges between 250 and 300 centigrade. Under this heat the copper unites with the sulfur and the larger part of the silicon of the silicid is made free in the form of an amorphous brownish-black powder.
- the mixture of sulfids and free silicon is treated with acids. I prefer boiling with diluted nitric acid. By these means all the copper is dissolved and most of the sulfur of the copper sulfid liberated.
- the silicon sulfid that may be present is decomposed'at the same time, yielding mainly silica and hydrogen sulfid.
- the copper salts are washed out and the residue is dried and extracted with carbon disulfid, which removes the sulfur.
- hydrofluoric I claim as my invention-- 1.
- the method herein specified of reclaiming the silicon in a free condition, consisting in finely pulverizing the silicon-copper alloy and mixing the same with sulfur, heating the same in a closed vessel to a temperature preferably between 250 and 300 centigrade, in which the copper unites with the sulfur and the silicon of the silicid is set free as an amorphous powder, substantially as set forth.
- the method herein specified of reclaiming the silicon in a free condition consisting in finely pulverizing the silicon-copper alloy and mixing the same with sulfur, heating the same in a closed vessel to a temperature preferably between 250 and 300 centigrade, in which the copper unites with the sulfur and the silicon of the silicid is set free as an amorphous powder, the amount of sulfur being regulated so as to obtain the compound Cu S or the compound CuS, substantially as set forth.
- the method herein specified of reclaiming the silicon in a free condition consisting in finely pulverizing the silicon-copper alloy and mixing the same with sulfur, heating the same in a closed vessel to a temperature preferably between 250 and 300 centigrade, in which the copper unites with the sulfur and the silicon of the silicid is set free as an amorphous powder, treating the mixture of sulfids and free silicon with acids to dissolve the copper and liberate the sulfur, decomposing the sulfids, Washing out the copper salts, drying the residue and extracting the sulfur by carbon disulfid and treating the remainder with hydrofluoric acid to remove the silica, substantially as set forth.
Description
ilnrrn STATES ATENT rrrcn.
GUILLAUME DE CHALMOT, OF HOLCOMB ROCK, VIRGINIA.
METHOD OF OBTAINING FREE. AMORPHOUS SILICON.
SPECIFICATION forming part of Letters Patent No. 602,632, dated April 19, 1898.
Application filed September 24., 1897.
To all whom it 777/602] concern.-
Be it known that I, GUILLAUME DE CHAL- MOT, a citizen of the United States, residing at Holcomb Rock, county of Bedford, and State of Virginia, have invented a new and useful Improvement in Methods of Obtaining Free Amorphous Silicon, of which the following is a specification.
In the process heretofore practiced by me of reducing silica or silicates in the presence of copper I have obtained crystalline alloys which consist of free copper, free silicon, and copper silicid, represented by the formula Cu si. By treating these crystalline alloys with acids a large proportion or all of the copper is dissolved, while the silicon that is combined with the copper is oxidized and forms silica. The crystalline silicon remains unaltered by this treatment, and it can be purified of the silica by dissolving the same in hydrofluoric acid. In this method of obtaining free silicon a part of the silicon that had been reduced from the silica could not be obtained in a free condition, and to this extent the former method was defective. This portion was that united to the copper and oxidized under the treatment with acids.
A copper-silicon alloy of average quality was found by chemical analysis to contain: copper, 70.05 per cent; iron, 0.87 per cent; free silicon, 19. 21 percent. combined silicon, 10.10 per cent.
The object of my present invention is to reclaim as large a portion as possible of the 10.10 per cent. of combined silicon and convert the same into free silicon, as it is apparent that heretofore more than one-third of the total percentage of silicon in the alloy was lost in the operation.
In carrying out the present process the alloy is finely ground and mixed with sufur, the quantity of sulfur being determined by the percentage composition of the alloy. This finely-ground mixture is heated in a closed vessel to a temperature which preferably ranges between 250 and 300 centigrade. Under this heat the copper unites with the sulfur and the larger part of the silicon of the silicid is made free in the form of an amorphous brownish-black powder.
If there is not enough sulfur employed,
some of the copper will remain in its union Serial No. 662,919. (No specimens.)
with the silicon, and if there is too much sulfur some of it will unite with the silicon, especially at places where the sulfur has run together into drops.
I have found that silicon is liberated if the amount of sulfur employed is just sufficient to form with all the copper the com pound Cu S, and that it is also liberated if twice as much sulfur is used, so that the compound C118 is formed; but in the latter case more of the silicon will combine with sulfur. Ihave also found that the higher the temperature is raised the more the silicon will combine with sulfur, but that at the temperatures named the reaction obtained is the most desirable.
Operating with a high-grade silicon alloy I obtained the following results: Before treatment: free silicon, 19.21 per cent; combined silicon, 10.10 per cent. After treatment with sulfur: 25.77 per cent. of original alloy and 3.54 per cent. of original alloy.
The following formula shows the result of treating a low-grade silicid with just enough. sulfur to obtain the compound C11 8: Before treatment: free silicon, 1.22 per cent; combined silicon, 11.74 per cent. After treatment with sulfur: 7.84 per cent. of original alloy and 5.12 per cent. of original alloy.
The following formula shows the result of treating a low-grade silicid with enough sulfur to produce the compound OuS: Before treatment: free silicon, 1.22 per cent; combined silicon, 11.74. per cent. After treatment with sulfur: 7.27 per cent. of original alloy and 5.69 per cent. of original alloy.
The mixture of sulfids and free silicon is treated with acids. I prefer boiling with diluted nitric acid. By these means all the copper is dissolved and most of the sulfur of the copper sulfid liberated. The silicon sulfid that may be present is decomposed'at the same time, yielding mainly silica and hydrogen sulfid. The copper salts are washed out and the residue is dried and extracted with carbon disulfid, which removes the sulfur.
The remainder is treated with hydrofluoric I claim as my invention-- 1. In the process of reducing silica or silicates in the presence of copper, the method herein specified of reclaiming the silicon in a free condition, consisting in finely pulverizing the silicon-copper alloy and mixing the same with sulfur, heating the same in a closed vessel to a temperature preferably between 250 and 300 centigrade, in which the copper unites with the sulfur and the silicon of the silicid is set free as an amorphous powder, substantially as set forth.
2. In the process of reducing silica or silicates in the presence of copper, the method herein specified of reclaiming the silicon in a free condition consisting in finely pulverizing the silicon-copper alloy and mixing the same with sulfur, heating the same in a closed vessel to a temperature preferably between 250 and 300 centigrade, in which the copper unites with the sulfur and the silicon of the silicid is set free as an amorphous powder, the amount of sulfur being regulated so as to obtain the compound Cu S or the compound CuS, substantially as set forth.
3. In the process of reducing silica or silicates in the presence of copper, the method herein specified of reclaiming the silicon in a free condition, consisting in finely pulverizing the silicon-copper alloy and mixing the same with sulfur, heating the same in a closed vessel to a temperature preferably between 250 and 300 centigrade, in which the copper unites with the sulfur and the silicon of the silicid is set free as an amorphous powder, treating the mixture of sulfids and free silicon with acids to dissolve the copper and liberate the sulfur, decomposing the sulfids, Washing out the copper salts, drying the residue and extracting the sulfur by carbon disulfid and treating the remainder with hydrofluoric acid to remove the silica, substantially as set forth.
Signed by me this 15th day of September, 1897.
G. DE Ol-IALMOT.
Witnesses:
GEO. T. LANCASTER, JOHN C. TEMPLE.
Publications (1)
Publication Number | Publication Date |
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US602632A true US602632A (en) | 1898-04-19 |
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US602632D Expired - Lifetime US602632A (en) | Method of obtaining free amorphous silicon |
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US (1) | US602632A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1003196B (en) * | 1952-02-13 | 1957-02-28 | Dr Hans Kautsky | Process for the production of finely divided silicon |
US2803521A (en) * | 1952-03-05 | 1957-08-20 | Wacker Chemie Gmbh | Method of treating spent metallic reaction masses from the direct process production of organohalosilanes |
US3396012A (en) * | 1965-10-04 | 1968-08-06 | Dow Chemical Co | Recovery of silicon from alloys thereof and from silicon sulfides |
-
0
- US US602632D patent/US602632A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1003196B (en) * | 1952-02-13 | 1957-02-28 | Dr Hans Kautsky | Process for the production of finely divided silicon |
US2803521A (en) * | 1952-03-05 | 1957-08-20 | Wacker Chemie Gmbh | Method of treating spent metallic reaction masses from the direct process production of organohalosilanes |
US3396012A (en) * | 1965-10-04 | 1968-08-06 | Dow Chemical Co | Recovery of silicon from alloys thereof and from silicon sulfides |
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