US979363A - Chemical process. - Google Patents
Chemical process. Download PDFInfo
- Publication number
- US979363A US979363A US393227A US1907393227A US979363A US 979363 A US979363 A US 979363A US 393227 A US393227 A US 393227A US 1907393227 A US1907393227 A US 1907393227A US 979363 A US979363 A US 979363A
- Authority
- US
- United States
- Prior art keywords
- carbon
- oxid
- reduction
- metal
- vacuum
- 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
- 238000001311 chemical methods and process Methods 0.000 title description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 34
- 229910052799 carbon Inorganic materials 0.000 description 27
- 230000009467 reduction Effects 0.000 description 18
- 229910052751 metal Inorganic materials 0.000 description 16
- 239000002184 metal Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 11
- 239000000203 mixture Substances 0.000 description 9
- 239000002245 particle Substances 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 239000006233 lamp black Substances 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000004020 conductor Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000003870 refractory metal Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 150000002736 metal compounds Chemical class 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 229910052721 tungsten Inorganic materials 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- 244000299461 Theobroma cacao Species 0.000 description 1
- 235000005764 Theobroma cacao ssp. cacao Nutrition 0.000 description 1
- 235000005767 Theobroma cacao ssp. sphaerocarpum Nutrition 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 235000001046 cacaotero Nutrition 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 150000001722 carbon compounds Chemical class 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910000765 intermetallic Inorganic materials 0.000 description 1
- 239000011872 intimate mixture Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 244000144985 peep Species 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- 239000003039 volatile agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C27/00—Alloys based on rhenium or a refractory metal not mentioned in groups C22C14/00 or C22C16/00
- C22C27/02—Alloys based on vanadium, niobium, or tantalum
- C22C27/025—Alloys based on vanadium, niobium, or tantalum alloys based on vanadium
Definitions
- My present invention relates to the treatment of metallic compounds, and my present a plication is a division of application, July 2, 1906.”
- Seria No. 324,408, filed by me My invention includes the reduction of metallic compounds in a vacuum or inert atmosphere, with the production of pure metal.
- the process of reduction may be closely watched by means of the manometer, for when reduction, begins, carbon monoxid 'is evolved and the gage reading increases, and
- the grains of carbon are too coarse, they leave centers or cores of carbon which have not been reached by the diffusing oxid. If the oxid is nonvolatile the reduction takes place only at the surface of contact between the grains of carbon and oxid, and hence complete reaction between the oxid and carbon to form a pure metal can only take place when the particles are very small.
- I first obtain a deposit of 'lamp' black from volatile hydrocarbons and I then heat the lamp black to a very high temperature in a vacuum to remove all gases and volatile hydrocarbons, or I may heat it to a temperature approximating perhaps. 3000 or 4000 degrees centigrade to graphitize the carbon.-
- the resultant product is an absolutely ure carbon in a fine state of division. much more perfect mixture of oxid and carbon can be obtained with this fired lamp black than with any other kinds of carbon with which I have worked, and furthermore, the reduction of oxids takes place more rapidly than with other forms of carbon.
- the metal obtained by the reduction of the oxid is in the form of grains having the same size and shape asthe original carbon particles; consequently,".by using lamp black, I can obtain the refractory 'metal in a. powdered form much finer than any that has heretofore been produced.
- a product consisting of finely divided refractory metal, the grains of which are pseudomorphs of graphitized lamp black.
- Powdered tungsten the grains of which are pseudomorphs of lamp black particles.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Description
UNITED STATES PAT NT OFFICE. I
WILLIAM C. ARSEM, OF- SCHENECTADY, YORK, ASSIGNOR- TO GENERAL'ELECTBIC COMPANY, A CORPORATION OF NEW YORK. V
CHEMICAL PROCESS.
Patented Dec. 20, 1910. Divided and this application filed September 16, 1907-. Serial No. 898,227.
To all whom it may concern:
Be it known that I, WILLIAM C. ARsEM, a citizen of the United States, residing at Schenectady, county of Schenectady, State of New York, useful Improvements in Chemical Processes, of which the following is a specification.
My present invention relates to the treatment of metallic compounds, and my present a plication is a division of application, July 2, 1906."
Seria No. 324,408, filed by me My invention includes the reduction of metallic compounds in a vacuum or inert atmosphere, with the production of pure metal.
In performing the reduction of the metallic compound I prefer to make use of the vacuum furnace shown in U. S. Patent No. 785,535, issued to, me March 21, 1905. This patent discloses a furnace of the resistance type in which the heating conductor is a helix of carbon provided with a central aperture through which a crucible may be introduced containing the charge to be treated. These parts are all inclosed in a vacuum tight metal case connected permanently with a vacuum pump and provided with external cooling means and other auxiliaries. The furnace is provided with a peep hole through which the reactions within may be observed, and the pump is provided with a manometer for indicating-the state of the vacuum within the furnace.
In carrying'out the first step of my process I mix a reducible compound of therefractory anetal, such as the oxid, with a finely divided reducing agent such as aluminum or carbon and I introduce this mixture into the crucible of the vacuum furnace, and after -exhausting the air I heat up thecharge until the desired reduction is effected. If a pure metal is desired I so proportion the charge that the carbon will be entirely used up in the reduction of the oxid without leaving a residue of unreduced oxid. In order to insure a good contact between the particles of carbon and of oxid I find it sometimes desirable to compress the mixture into briquets;
or lumps. This intimate contact between the particles facilitates the reaction.
The process of reduction may be closely watched by means of the manometer, for when reduction, begins, carbon monoxid 'is evolved and the gage reading increases, and
have invented certain new and "stem, tantalum,
after the completion of the reduction the carbon monoxid ceases to be formed and the vacuum ra idl improves. The vacuum pump is maintained in operation throughout the run, and the pressure within the inclosure never exceeds a few millimeters of mercury. By the above method of procedure I may reduce the oxids, sulfids, or other compounds, of such refractory metals as tungvanadium, or molybdenum, and obtain the metal in a pure state.
I am aware that it has been heretofore proposed to reduce the oxids of some of these metals with carbon in an arc furnace in the open air, but the method I have above out lined possesses many advantages and yields a superior product. In an arc furnace the temperature is variable and not easily controlled and the metal becomes fused and, unless a large excess of oxid is used, takes up carbon. In the vacuum furnace, the ease 0 temperature control makes possible the reduction of the oxid at a temperature lower than the melting point of the metal. Contamination with graphite is thus avoided and the unfused owder is much more pure than would be tlie case if fusion had occurred. The metal is ordinarily obtained in a coherent block. In a vacuum, oxidation by air is not possible, and the work may be carried on with accurately weighed quantities. By proper adjustment of the amounts of carbon and metallic oxid, an exceptionally pure metal may be produced.
In addition to the advantages above pointed out, it should be noted that reduction in cacao may take place at a temperature lower than the same reduction would take place at atmospheric pressure. This is probably due to the fact that when the surrounding medium is of low density, as in the vacuum, the reducible substance vaporizes and comes into chemical contact with carbon at a lower temperature. I
From this description of my process it will be understood that the material to be reduced is heated by radiant heat given out by a resistance conductor within the furnace. The reducible material is nevertraversed by current, and is, therefore never subjected to the sintering or fusing action which sometimes takes place when current passes through a' powder; a fusing action probably due to minute arcs between adjacent and poorly contacting particles. By the use of thing which contributes materially to t e purity of the product is of importance.
In the general rocess above outlined I have referred to t e use of carbon as a reducing agent and I now desire to point out certain advantages which arise from using this carbon in an exceedingly fine state of sub-division. In reducing metals from their oxids by carbon the purity of the roduct as regards freedom from carbon e ends both on the vapor pressure of the oxid at the reduction temperature and also on the size of the particles of carbon. If theoxid is volatile and the metal does not fuse at the reduction temperature, each grain of metal is a pseudomorph of a grain of carbon, since the metal is produced when the vapor of the oxid difli'uses into the carbon particles. Hence, if the grains of carbon are too coarse, they leave centers or cores of carbon which have not been reached by the diffusing oxid. If the oxid is nonvolatile the reduction takes place only at the surface of contact between the grains of carbon and oxid, and hence complete reaction between the oxid and carbon to form a pure metal can only take place when the particles are very small.
' To secure carbon in a very finely divided condition I first obtain a deposit of 'lamp' black from volatile hydrocarbons and I then heat the lamp black to a very high temperature in a vacuum to remove all gases and volatile hydrocarbons, or I may heat it to a temperature approximating perhaps. 3000 or 4000 degrees centigrade to graphitize the carbon.- The resultant product is an absolutely ure carbon in a fine state of division. much more perfect mixture of oxid and carbon can be obtained with this fired lamp black than with any other kinds of carbon with which I have worked, and furthermore, the reduction of oxids takes place more rapidly than with other forms of carbon.
. As previously stated, the metal obtained by the reduction of the oxid is in the form of grains having the same size and shape asthe original carbon particles; consequently,".by using lamp black, I can obtain the refractory 'metal in a. powdered form much finer than any that has heretofore been produced.
What I claim as new and desire to secure by Letters Patent of the United States, is, v 1. The process which consists in reducing a metal compound in a vacuum by heat treatmentwhile in contact with graphitized lamp black.
2.' The process which consists in mechanically mixing a finely divided refractory metallic oxid with carbon deposited from a volatile compound and subsequently fired, and heating said mixture to cause a reduction of said metal compound.
3. The process which consists in producing a carbonaceous deposit from a volatile carbon compound, heating said deposit to produce pure graphite in a finely divided' condition, mixing said gra hite with a reducible compound, and heating said mixture in a vacuum to effect reduction.
4. The process which consists in mixing an oxid of tungsten with a dry powdered reducing agent and then heating said mixture in a vacuum by radiant heat to cause reduction of said oxid.
5. The process which consists in forming an intimate mixture of a powdered reducing agent and a refractory metal oxid, and heatin said mixture to a reducing temperature in a vacuum by means of a resistance conductor insulated. from said mixture.
6. A product consisting of finely divided refractory metal, the grains of which are pseudomorphs of graphitized lamp black.
. 7. Powdered tungsten the grains of which are pseudomorphs of lamp black particles.
In witness whereof, I have hereunto set my hand this 13th day of September, 1907.
WILLIAM C. ARSEM.
Witnesses BENJAMIN B. HULL,
MARGARET E. WOOLLEY.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US393227A US979363A (en) | 1906-07-02 | 1907-09-16 | Chemical process. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US1906324408A | 1906-07-02 | 1906-07-02 | |
| US393227A US979363A (en) | 1906-07-02 | 1907-09-16 | Chemical process. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US979363A true US979363A (en) | 1910-12-20 |
Family
ID=3047739
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US393227A Expired - Lifetime US979363A (en) | 1906-07-02 | 1907-09-16 | Chemical process. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US979363A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2556912A (en) * | 1946-09-14 | 1951-06-12 | Gardner Daniel | Thermal process for producing pure tantalum and columbium compounds |
| US2834671A (en) * | 1954-05-13 | 1958-05-13 | John S Nachtman | Method of producing molybdenum |
| US2839379A (en) * | 1955-08-19 | 1958-06-17 | Union Carbide Corp | Metal aggregate |
| US2850378A (en) * | 1956-12-17 | 1958-09-02 | Walter M Weil | Production of chromium by low-pressure reduction of oxides |
| US2982014A (en) * | 1955-05-20 | 1961-05-02 | Meyer-Hartwig Eberhard | Process of manufacturing ceramic compounds and metallic ceramic compounds |
| US3020151A (en) * | 1957-02-26 | 1962-02-06 | John S Nachtman | Beneficiation and recovery of metals |
| US3107165A (en) * | 1961-10-12 | 1963-10-15 | Nat Res Corp | Purification of tantalum metal by reduction of the oxygen content by means of carbon |
-
1907
- 1907-09-16 US US393227A patent/US979363A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2556912A (en) * | 1946-09-14 | 1951-06-12 | Gardner Daniel | Thermal process for producing pure tantalum and columbium compounds |
| US2834671A (en) * | 1954-05-13 | 1958-05-13 | John S Nachtman | Method of producing molybdenum |
| US2982014A (en) * | 1955-05-20 | 1961-05-02 | Meyer-Hartwig Eberhard | Process of manufacturing ceramic compounds and metallic ceramic compounds |
| US2839379A (en) * | 1955-08-19 | 1958-06-17 | Union Carbide Corp | Metal aggregate |
| US2850378A (en) * | 1956-12-17 | 1958-09-02 | Walter M Weil | Production of chromium by low-pressure reduction of oxides |
| US3020151A (en) * | 1957-02-26 | 1962-02-06 | John S Nachtman | Beneficiation and recovery of metals |
| US3107165A (en) * | 1961-10-12 | 1963-10-15 | Nat Res Corp | Purification of tantalum metal by reduction of the oxygen content by means of carbon |
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