US2033172A - Process for the manufacture of alloys containing boron - Google Patents
Process for the manufacture of alloys containing boron Download PDFInfo
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- US2033172A US2033172A US681212A US68121233A US2033172A US 2033172 A US2033172 A US 2033172A US 681212 A US681212 A US 681212A US 68121233 A US68121233 A US 68121233A US 2033172 A US2033172 A US 2033172A
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
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- PRO SSSS FOR THE MANUFACTURE OF ALLOYS CONTAINING BORON Filed July 19, 1953 Z73 if?) 557 Z RZ J Z: i :1; iii? Z ⁇ 7 1 IMW I LwQM supplying device.
- the present invention relates to the manufacture of alloys containing boron. Itconstitutes an improvement in the FrenchPatent No. 638,345 of 1st December 1926 and of the twoadditions No. 34,495 of 1st October 1927, and No. 37,559 01- '17th June 1929. g
- the metal or the alloy 1 into which it is proposed to introduce boron can be employed in the solid state asvcathode, that the actual alloy is obtained in the fused state at as low a temperature as possible and that it can be collected by casting without interrupting the progress of the operation so that the manufacture of molten boron-alloys is ensured by a continuousprocess.
- the baths employed can have among others the following molecular compositions:
- the electrolysis is preferably effected in vats of carbon with central, anodes likewise of car'- ban, the vat being connected to the negative pole of the source of current so as to serve as
- the boron liberated in the electrolysis becomes fixed on the metallic cathode thus giving an alloy which fuses and flows when its content of boron is in the neighbourhood 01' that of the eutectic alloy; the composition of the alloy formed is thus to some degree a function of the temperature of electrolysis and it-is necessary that this temperature should remain practically constant.
- the alloy fuses and flows to the bottom of the vat and can be drawn oil without interrupting the operation.
- Such an alloy obtained at 1050 C. can in addition, during its period of remaining at the bottom of the vat, be enriched up to-16% of boron.
- the process gives not only excellent results in the manufacture of the boron-nickel alloys (with 10-16% of boron), but also in that of boroncobalt alloys which can be obtained under the 20 same conditions and with the same contents of boron. It can be applied with success to the, preparation of other alloys of the metals with boron, even when the eutectics of thesealloys are formed. at more elevated temperatures.
- it is possible to prepare the. alloys of iron and boron by employing cathodes of iron or castiron and by effecting the electrolysis at a temperature of about 1300 C.
- these alloys do not contain large quantities of carbon, silicon or oi the reducing element as in the case of those prepared by the electro-thermal method.
- plates or sheets metals correspondconstituted by the alloy into which it is proposed to introduce the boron.
- nickel-chromium-boron or iron-nickel-chromium-boron etc.. which can contain up to 16% of boron.
- the metal or the alloy of the cathode is in fact employed in the solid state in are arranged vertically between the anode and the interior walls of the carbon vat and rest on the bottom of this latter which alone is connected directly to the negative pole of the source of current.
- bars When bars are employed these can also be inclined in such a manner that their lower extremities are placed under the central anode.
- the accompanying drawing represents diagrammatically a vat for the manufacture of alloys containing boron arranged in accordance with the said characteristic.
- the metallic bars descend under their own weight and remain in contact with the bottom of the vat; in order to maintain them in position the vat is in -part covered by a plate pierced with holes or by a grid into which the bars are placed.
- the alloy formed at the commencement of the operation collects at the bottom of the vat where it forms a liquid layer. It results from this arrangement that in the course of the operation the cathodic surface is constituted on the one hand by the solid platesor bars and on the other hand by the liquid alloy at the bottom of the vat into which the bars plunge, all devicesjor suspension and connection of these bars being thus eliminated.
- a continuous electrolytic process for producing molten alloys containing'boron, and having a composition approximating a predetermined eutectic which consists in: immersing the metal to be alloyed in a bathcomposed of boric anhydride or borates in a fused state; utilizing said metal as a cathode; maintaining a supply of the boron compound in said bath; maintaining the temperature of said bath close to the fusing-temperature of said eutectic and not below said fusing temperature; and drawing off the molten product thus formed while continuing the electrolytic process.
Description
7 March 10, 1936. J. L. AN'DRIEUX 2,033,172
PRO SSSS FOR THE MANUFACTURE OF ALLOYS CONTAINING BORON Filed July 19, 1953 Z73 if?) 557 Z RZ J Z: i :1; iii? Z\\\ 7 1 IMW I LwQM supplying device.
Patented Mar. 10, 1936 PATENT OFFICE 2,033.17: raoccss roa THE MANUFACTURE or armors comma aonon .lean Lucien Andrienx, Grenoble, France, asslgnor to Socit dElectrochimie, dElectrometallurgle et des Acieries' Elcctriques dUglne. Paris,
France, a corporation of France Application July 19, 1933, Serial No. 681,212
In France July 21, 1932 3 Claims. (01. 294-19) The present invention relates to the manufacture of alloys containing boron. Itconstitutes an improvement in the FrenchPatent No. 638,345 of 1st December 1926 and of the twoadditions No. 34,495 of 1st October 1927, and No. 37,559 01- '17th June 1929. g
\ It consists essentially in producing the alloys in question directly by electrolyzing by means of metallic cathodes, a bath constituted, as in the case of'the parent patent and the additions above mentioned, by boric anhydride or borates in the fused state with the addition in most cases of halogen-salts of alkalies or alkaline earths (for example fluorides), the operating being conducted at a temperature slightly above the melting point of the eutectic having a composition in a neighbourhood of that 01' the alloy which it is desired to Obtain.
The notable result is that the metal or the alloy 1 into which it is proposed to introduce boron can be employed in the solid state asvcathode, that the actual alloy is obtained in the fused state at as low a temperature as possible and that it can be collected by casting without interrupting the progress of the operation so that the manufacture of molten boron-alloys is ensured by a continuousprocess.
The baths employed can have among others the following molecular compositions:
It is advantageous for the good progress of the process to maintain the proportions of the constituents of the electrolytic bath practically constant by additions of boric anhydride or-oi' the other substances decomposed.
The electrolysis is preferably effected in vats of carbon with central, anodes likewise of car'- ban, the vat being connected to the negative pole of the source of current so as to serve as The boron liberated in the electrolysis becomes fixed on the metallic cathode thus giving an alloy which fuses and flows when its content of boron is in the neighbourhood 01' that of the eutectic alloy; the composition of the alloy formed is thus to some degree a function of the temperature of electrolysis and it-is necessary that this temperature should remain practically constant.-
current duction ofnickel-boron alloys. The nickel, the point-mi fusion'of which is 1450 C., formswith the boron, which fuses atabout 2300 0., several 1 eutectics of which the most fusible contains 12.5% of boron and melts at 990 C. 5
In utilizing solid nickel as cathode for the elecx trolysls, at about 1050 0., of one of the above baths, boron is separated and becomes fixed on thenickel.
The alloy fuses and flows to the bottom of the vat and can be drawn oil without interrupting the operation.
Such an alloy obtained at 1050 C. can in addition, during its period of remaining at the bottom of the vat, be enriched up to-16% of boron.
The process gives not only excellent results in the manufacture of the boron-nickel alloys (with 10-16% of boron), but also in that of boroncobalt alloys which can be obtained under the 20 same conditions and with the same contents of boron. It can be applied with success to the, preparation of other alloys of the metals with boron, even when the eutectics of thesealloys are formed. at more elevated temperatures. Thus, for example, it is possible to prepare the. alloys of iron and boron by employing cathodes of iron or castiron and by effecting the electrolysis at a temperature of about 1300 C. I
Being obtained electrolytically these alloys do not contain large quantities of carbon, silicon or oi the reducing element as in the case of those prepared by the electro-thermal method.
The process permits likewise of preparing ternary or more complex alloys. For this purpose it is possible to operate in several ways for example: Y
1. By adding to the electrolysis vat in which the first alloy is formed in the fused-state, the
metal (copper, zinc, aluminium etc. or the 40 metals which it is proposed to introduce into the final alloy, this addition being capable in some cases of facilitating the casting of the product, 21By adding to the electrolytic bath suitable quantities of an oxide or oi a salt (salt containing. orwgen or halogen) of the metal (or metals) to be alloyed with the metal of the cathode and the boron. a Thus for example by adding to the electrolysis 50 baths small quantities of oxideof chromium, tungsten, molybdenum, vanadium, titanium, aluminium or-beryllium etc., there are obtained with cathodes o nickel (or cobalt) ternary alloys containing wit the nickel (or cabolt) and the 5 boron small quantities of the ing to the oxides added.
3. By taking as cathode bars, plates or sheets metals correspondconstituted by the alloy into which it is proposed to introduce the boron.
For example by employing bars a of ferro-nickel,
'ferro-cobalt, nickel-chromium or ferro-nickelchromium etc., there are obtained respectively .alloys of i'ron-nickel-boron, iron-cobalt-boron,
nickel-chromium-boron or iron-nickel-chromium-boron etc.. which can contain up to 16% of boron.
One of the best modes of application of the process is characterized by the particular arrangement which it is advantageous to give to the cathode. The metal or the alloy of the cathode is in fact employed in the solid state in are arranged vertically between the anode and the interior walls of the carbon vat and rest on the bottom of this latter which alone is connected directly to the negative pole of the source of current. When bars are employed these can also be inclined in such a manner that their lower extremities are placed under the central anode.
The accompanying drawing represents diagrammatically a vat for the manufacture of alloys containing boron arranged in accordance with the said characteristic.
the form of sheets, plates, grids or bars which In the drawing I is. the vat, I the central anode, 3 the metallicbars, 4 the electrolytic bath and 5 the alloy produced in the fused state, 5' being the casting hole.
In proportion as they are attacked the metallic bars descend under their own weight and remain in contact with the bottom of the vat; in order to maintain them in position the vat is in -part covered by a plate pierced with holes or by a grid into which the bars are placed.
The alloy formed at the commencement of the operation collects at the bottom of the vat where it forms a liquid layer. It results from this arrangement that in the course of the operation the cathodic surface is constituted on the one hand by the solid platesor bars and on the other hand by the liquid alloy at the bottom of the vat into which the bars plunge, all devicesjor suspension and connection of these bars being thus eliminated.
It likewise results therefrom that theactive surface of the bars or the plates is constantly re-' newed, that the alloy formed flows slowly of! becoming collected at the surface of the liquid alloy which surface on account of this fact is likewise renewed. This continuous renewal of the entire active cathodic surface favours the formaduces the wear.
in: immersing the metal to be alloyed in a bath composed of boric anhydride or borates in a fused state; utilizing said metal as a cathode in carrying on the electrolytic process; maintaining the proportions of the constituents of the bath substantially constant; maintaining the temperature of the bath substantially constant and at least at the melting point of the eutectic formed by the metal and the boron, but below the melting point of the metal; and drawing off the molten product thus formed while continuing the electrolytic process.- i 2. A. continuous electrolytic process for producing molten alloys containing boron which comjii'iSEEfifiiihfilhg, in a bath containing fused boric anhydride or borates, the lower portion of an elongated cathode containing the metal to bev alloyed, arranged tcrfeed by gravity into said bath to compensate for removal of said metal from the cathode; maintaining a supply of the boron comp und in said bath; maintaining the bath at a temperature between the melting-point of'the eutectic formed by the boron and said metal arid the melting point of said metal; and drawing ofl! the molten alloy thus formed while continuing the electrolytic process. c
3. A continuous electrolytic process for producing molten alloys containing'boron, and having a composition approximating a predetermined eutectic, which consists in: immersing the metal to be alloyed in a bathcomposed of boric anhydride or borates in a fused state; utilizing said metal as a cathode; maintaining a supply of the boron compound in said bath; maintaining the temperature of said bath close to the fusing-temperature of said eutectic and not below said fusing temperature; and drawing off the molten product thus formed while continuing the electrolytic process.
- JEAN LUCIEN ANDRIEUX.
Applications Claiming Priority (1)
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FR2033172X | 1932-07-21 |
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US2033172A true US2033172A (en) | 1936-03-10 |
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US681212A Expired - Lifetime US2033172A (en) | 1932-07-21 | 1933-07-19 | Process for the manufacture of alloys containing boron |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2431723A (en) * | 1942-01-17 | 1947-12-02 | Leland A Yerkes | Electrolytic method for producing magnesium alloys |
US3024175A (en) * | 1959-08-04 | 1962-03-06 | Gen Electric | Corrosion resistant coating |
US3024176A (en) * | 1959-08-04 | 1962-03-06 | Gen Electric | Corrosion resistant coating |
US3024177A (en) * | 1959-08-04 | 1962-03-06 | Gen Electric | Corrosion resistant coating |
US3912827A (en) * | 1973-11-13 | 1975-10-14 | Toyota Chuo Kenkyusko Kk | Method for forming a chromium carbide layer on the surface of an iron, ferrous alloy or cemented carbide article |
US20100294670A1 (en) * | 2009-05-19 | 2010-11-25 | Colorado School Of Mines | Synthesis of boron using molten salt electrolysis |
US20110132769A1 (en) * | 2008-09-29 | 2011-06-09 | Hurst William D | Alloy Coating Apparatus and Metalliding Method |
-
1933
- 1933-07-19 US US681212A patent/US2033172A/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2431723A (en) * | 1942-01-17 | 1947-12-02 | Leland A Yerkes | Electrolytic method for producing magnesium alloys |
US3024175A (en) * | 1959-08-04 | 1962-03-06 | Gen Electric | Corrosion resistant coating |
US3024176A (en) * | 1959-08-04 | 1962-03-06 | Gen Electric | Corrosion resistant coating |
US3024177A (en) * | 1959-08-04 | 1962-03-06 | Gen Electric | Corrosion resistant coating |
US3912827A (en) * | 1973-11-13 | 1975-10-14 | Toyota Chuo Kenkyusko Kk | Method for forming a chromium carbide layer on the surface of an iron, ferrous alloy or cemented carbide article |
US20110132769A1 (en) * | 2008-09-29 | 2011-06-09 | Hurst William D | Alloy Coating Apparatus and Metalliding Method |
US20100294670A1 (en) * | 2009-05-19 | 2010-11-25 | Colorado School Of Mines | Synthesis of boron using molten salt electrolysis |
US8287715B2 (en) * | 2009-05-19 | 2012-10-16 | Colorado School Of Mines | Synthesis of boron using molten salt electrolysis |
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