US2022404A - Method for the manufacture of beryllium and alloys - Google Patents
Method for the manufacture of beryllium and alloys Download PDFInfo
- Publication number
- US2022404A US2022404A US732436A US73243634A US2022404A US 2022404 A US2022404 A US 2022404A US 732436 A US732436 A US 732436A US 73243634 A US73243634 A US 73243634A US 2022404 A US2022404 A US 2022404A
- Authority
- US
- United States
- Prior art keywords
- beryllium
- fluoride
- fluorides
- bath
- alkali
- 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
Classifications
-
- 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
- C25C3/34—Electrolytic production, recovery or refining of metals by electrolysis of melts of metals not provided for in groups C25C3/02 - C25C3/32
Definitions
- NazBeFl is too low in tent to yield well-operating electrolytic such baths are too easily subject to anode effect", particularly when in association with any excess NaF over that present in the NaaBeFi itseli.
- ammonium beryllium fluoride properly used, offers an almost ideal source of electrolyzable beryllium.
- the additions, for the most part, of ammonium beryllium fluoride have been to baths predominant in alkali earth fluorides, with high operating temv peraturesspecifically, at or above the melting (1280" 0.).
- the proportion of BeFz in the bath can be raised sufliciently above the point where anode effect objectionably sets in so that this unhappy factor does not present itself
- the ammonium beryllium fluoride should be slowly added to the fused bath to avoid objectionable agitation.
- any single fluoride or mixture of fluorides more electropositive than beryllium will do for the purpose.
- the only requirement is that the fusion bath be freely fluid and electrolyzable at a temperature below the melting point of beryllium.
- the process of obtaining elementary beryllium which includes the steps of adding ammonium beryllium fluoride to a fusion of the fluorides of one or more metals more electropositive than beryllium, and subjecting the mixed fusion to electrolysis at a temperature below the melting point of beryllium.
Description
Patented N... 26, 1935 UNITED STATES 2,022,404 METHOD FOR THE MANUFACTURE OF BERYLLIUM AND ALLOYS Harry G. Claflin, Marysville, Mich, assignor to The Beryllium Corporation,
New York, N. Y.,
a corporation of Delaware No Drawing.
Application June 26, 1934, Serial No. 732,436
8 Claims. (01. 204-19) This invention relates to a method for the convenient and economical manufacture of beryllium. It is useful in the production of elementary beryllium and may effectively .be employed as part of a process for the production or continuous production of alloys of beryllium.
Themarliest methods for the isolation of beryllium were thermal in nature, the alkali metals being used to reduce berylliumhalides, such as the chloride or the double alkali beryllium fluoride. Later, electrolytic eiforts hinged around the decomposition of the alkali beryllium fluorides, such as NazBeF4; in more recent times, electrolytic operations have centered about double fluoride mixtures higher in beryllium content, such as NaF.2BeFz, and about the anhydrous BeClz. The last mentioned has one great advantage over all other materials hitherto suggested as initial material for electrolytic operations: It permits there is nothing to build up in the electrolytic bath; full decomposition of the added substance, BeCln, occurs, and the bath returns to its original state, ready for further additions of the electrolyzable substance. However, anhydrous BeCl: is quite diflicult-and costly of manufacture, requiring the heating of normal beryllium compounds in the. simultaneous presence of chlorinating and reducing agents; this has made its use on a commercial scale quite expensive,-though technically it is admirable in most respects.
As for the fluorine compounds of beryllium, when combined with alkali fluorides in molecular compounds they have beenfar easier and less expensive to manufacture, but they sufier from the fact that continuous operation is impossible. Addition of NazBeF to an electrolysis bath, for example, results in the release pf Be at the cathode and half of the total added fluorine at the anode, but there is meanwhile a continuous build ing up of NaF in increasing amount of NaF in the bath makes continued operation impossible.
Moreover, NazBeFl is too low in tent to yield well-operating electrolytic such baths are too easily subject to anode effect", particularly when in association with any excess NaF over that present in the NaaBeFi itseli.
, Pure BeFz, while theoretically far more desirable than any double fluoride-since, like BeClz, it would leave nothing in the bath after electrolysis of the beryllium content-has hitherto been practically unknown as a chemical entity, because of beryllium conof continuous operation, since that the double point of beryllium the bath.- SoOner or later, the
baths;
at all in normal operation.
great idifliculties in its isolation. Evaporation of an aqueous solution containing only BeFz leaves nothing but a gummy basic mixture (frequently termed the oxyfluoride) even repeated evaporation with excess HF merely changesthe ratio of 5 basicity; fluorinecontent.
Aside from direct union of beryllium and fluorine, and reaction of dry HF on beryllium metal, there has hitherto been known only one procedure for making pure BeF2-thermal decomposition of the double ammonium beryllium fluoride, in accordance with the reaction:
Experience with the of beryllium fluoride in elecfluoride as a source trolyses has hitherto been quite discouraging and devoid of hopeiulness. And, because of the previous failure, under the conditions tried, of this double ammonium beryllium fluoride as a source of electrolyzable material,-it has been assumed that no'convenient method exists for, utilizing BeFz as electrolytic material.
Contrary to all such past beliefs, I have found ammonium beryllium fluoride, properly used, offers an almost ideal source of electrolyzable beryllium. In the past, the additions, for the most part, of ammonium beryllium fluoride have been to baths predominant in alkali earth fluorides, with high operating temv peraturesspecifically, at or above the melting (1280" 0.). Under the conditions of such high temperature operation, various factors appear as interference, among them reaction between the liberated ammonia (NH4F=NHa+I-IF) and the metallic beryllium.
I have found that, in electrolytic operations held below the melting point of beryllium" and preferably below 1000 C. (with the metal consequently appearing as flakes or spangles instead of as a molten regulus) the direct addition of ammonium beryllium fluoride does not cause such undesired reactions. I find that, by adding this compound to a bath preferably of sodium or other alkali fluoride, decomposition of the double compound takes place; and, as a result, there is formed in the batlea mutually soluble mixture of the alkali fluoride and beryllium fluoride, which can be varied in the matter of ratio of components, as desired. In this way, the proportion of BeFz in the bath can be raised sufliciently above the point where anode effect objectionably sets in so that this unhappy factor does not present itself The ammonium beryllium fluoride should be slowly added to the fused bath to avoid objectionable agitation.
Instead of using a single alkali fluoride as the preliminary operating fusion bath, I can use equally well, mixtures of the alkali fluorides, as well as mixtures of these with alkaline earth fluorides. Indeed, any single fluoride or mixture of fluorides more electropositive than beryllium will do for the purpose. The only requirement is that the fusion bath be freely fluid and electrolyzable at a temperature below the melting point of beryllium. For reasons of convenience and comfort of operation, I prefer to operate with the alkali fluorides, which permit electrolysis to proceed smoothly in the 600 C.-800 C. range.
This invention works particularly well in conjunction with the electrolytic process divulged in application of J. B. Arnold and myself, Serial No. 732,435, flled June 26, 1934, for the manufacture of alloys of beryllium with heavier metalssuch as copper, wherein massive metal cathodes are employed. In such use, higher temperatures are usually needed say from 900 C. to 1000 C. in the case of copper. When used with massive copper cathodes, for example, the inventions of appli-' cation Serial No. 732,435 and of this application, yield a continuous flow of liquid copper-beryllium alloy of about 2% to about 6% beryllium content.
Having described my invention, I claim:-
1. In the electrolytic production of beryllium, the steps of adding ammonium beryllium fluoride to a fusion of the fluorides of one or more metals more electropositive than beryllium, and of electrolyzing at atemperature below the melting point of beryllium.
2. The process of obtaining elementary beryllium which includes the steps of adding ammonium beryllium fluoride to a fusion of the fluorides of one or more metals more electropositive than beryllium, and subjecting the mixed fusion to electrolysis at a temperature below the melting point of beryllium.
3. In the electrolytic production of beryllium, the steps of adding ammonimn beryllium fluoride to a bath of a fluoride of one or more metals 5 more electropositive than beryllium, and of electrolyzing at a temperature below the melting point of beryllium.
4.In the electrolytic production of beryllium, the steps of adding ammonium beryllium fluoride 10 to a bath of a fluoride of one or more metals more electropositive than beryllium, and of electrolysing at a temperature below the melting point of beryllium, and preferably below1000 C.
5. The process of forming fused mixtures of 15 beryllium fluoride and the fluorides of one or. more metals more electropositive than beryllium which includes the steps of slowly or gradually adding ammonium beryllium fluoride to a fusion of the other fluoride or fluorides and of holding 20 the temperature below the melting point of beryllium.
6. The process of forming fused mixtures of beryllium fluoride and the fluorides of one or more alkali metals which includes the steps of 25 slowly or gradually adding ammonium beryllium fluoride to a fusion of the alkali fluoride or fluorides, and of holding the temperature below the melting point ofberyllium.
7. The process of forming fused mixtures of 30 beryllium fluoride and sodium fluoride which includes the steps of slowly or gradually adding ammonium beryllium fluoride to a fusion of sodium fluoride and of holding the temperature below the melting point of beryllium.
8. In the electrolytic production of beryllium, the steps of adding ammonium beryllium fluoride to a fusion of the fluorides of one or more alkali metals, and of electrolyzing at a temperature below the melting point of beryllium.
40 HARRY C. CLAFLIN.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US732436A US2022404A (en) | 1934-06-26 | 1934-06-26 | Method for the manufacture of beryllium and alloys |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US732436A US2022404A (en) | 1934-06-26 | 1934-06-26 | Method for the manufacture of beryllium and alloys |
Publications (1)
Publication Number | Publication Date |
---|---|
US2022404A true US2022404A (en) | 1935-11-26 |
Family
ID=24943497
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US732436A Expired - Lifetime US2022404A (en) | 1934-06-26 | 1934-06-26 | Method for the manufacture of beryllium and alloys |
Country Status (1)
Country | Link |
---|---|
US (1) | US2022404A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3257296A (en) * | 1964-05-08 | 1966-06-21 | Berghaus Bernhard | Process for obtaining metals by fusion electrolysis |
-
1934
- 1934-06-26 US US732436A patent/US2022404A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3257296A (en) * | 1964-05-08 | 1966-06-21 | Berghaus Bernhard | Process for obtaining metals by fusion electrolysis |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2022404A (en) | Method for the manufacture of beryllium and alloys | |
US2734855A (en) | Electrolytic preparation of reduced | |
US2731402A (en) | Production of metallic titanium | |
US2848396A (en) | Electrochemical preparation of boron | |
US1854684A (en) | Production of aluminum | |
US1740857A (en) | Process for the production of metallic beryllium | |
US1464625A (en) | Electrolyte for aluminum production and method of preparing same | |
US2841541A (en) | Chemical composition for chromium plating | |
US2774729A (en) | Recovery of uranium by electrolysis of a fused bath | |
US2892762A (en) | Production of elemental boron electrolytically | |
US1888118A (en) | Production of fluorine | |
US2810683A (en) | Production of elemental boron by fused salt electrolysis | |
US2876180A (en) | Fused salt bath for the electrodeposition of transition metals | |
US1960700A (en) | Method of making magnesium alloys | |
US2422590A (en) | Production of fluorine | |
US1861656A (en) | Process for producing beryllium metal | |
US2487214A (en) | Fused pyrosulfate-halide solvent electrolyte | |
US2243165A (en) | Recovery of tin | |
GB713446A (en) | A process for preparing titanium metal | |
US2159878A (en) | Process for the recovery of magnesium | |
US1809442A (en) | Process for the manufacture of metallic beryllium or its alloys | |
US362441A (en) | X e eichaed geatzel | |
GB794518A (en) | Metallic halides | |
SU38786A1 (en) | Method for producing metallic tantalum powder by electrolysis of molten salts | |
GB791151A (en) | Fused salt bath for the electrodeposition of the polyvalent metals titanium, niobium, tantalum and vanadium |