US2281235A - Process of fusing beryllium chloride - Google Patents
Process of fusing beryllium chloride Download PDFInfo
- Publication number
- US2281235A US2281235A US367623A US36762340A US2281235A US 2281235 A US2281235 A US 2281235A US 367623 A US367623 A US 367623A US 36762340 A US36762340 A US 36762340A US 2281235 A US2281235 A US 2281235A
- Authority
- US
- United States
- Prior art keywords
- chloride
- beryllium
- beryllium chloride
- cylinder
- fusing
- 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
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F3/00—Compounds of beryllium
Definitions
- This invention relates to the production of fused beryllium chloride.
- An object of this invention is to make a form of anhydrous beryllium chloride that is less reactive with the atmosphere than has been possible with the formation of beryllium chloride according to the prior art.
- Another object is to effect a fused form of beryllium chloride.
- Still another object is to produce a form of beryllium chloride particularly effective for easy and economical production of berylliumthenefrom.
- the drawing represents an illustrative diagrammatic section of the apparatus with which the method of this invention is practised.
- anhydrous beryllium chloride in the manufacture of pure beryllium metal the common method is the electrolysis of anhydrous beryllium chloride in a suitable fused salt bath.
- the anhydrous chloride is made by the chlorination of the oxide or other oxy-compound of beryllium, usually at a temperature between 800 C. and 1000 C.
- the cylinder l is permanently closed at the bottom end. At its top the cylinder has a removable cap 2 held tightly in place by any convenient means, as for instance, the bolts 3 and the flange l. Drilled through the cap 2 is a hole 5 into which is screwed a short piece of pipe t. At its other end the pipe 6, carries a valve 1, which in turn communicates with a shortpiece of pipe 8, used to carry away efiluent gases. If desired the valve I may be an automatic check valve preventing gases from travelling inward toward the cylinder.
- This liner also comprises a cylinder closed at the bottom only. This liner fits loosely into'the cylinder l with its bottom resting on the bottom of the cylinder.
- the liner 9 is filled with the ordinary fiuiiy beryllium chloride 90, in the'iorm in which it comes from the chlorinator. This chloride is tamped in place to increase the content as much as is conveniently possible.
- the liner has been filled and placed in the cylinder, the cap 2 is securely fastened in place.
- the whole assembly is then placed in any suitable furnace such as is describedbelow and After a little while when the interior of the its liquid phase and is not easily obtainable under ordinary conditions, the melting of it is not normally either a simple or an easy procedure,
- valve 1 has reached a temperature of about 100 0., fumes will start to be emitted from the point the valve 1 may be closed tightly without risk of building up any dangerous pressure in the cy inde
- the at g s continu d for a time longer, to make sure that all parts of the cylinder have reached a temperature of about 400 0., but without greatly exceeding that temperature.
- the valve 1 is tightly closed before the furnace is opened, in any case. and-certainly before any drop in temperature is permitted internally of the cylinder i. t
- the cylinder is now removed from the furnace and permitted to cool.
- the cap 2 is then removed and'the liner 9, with its contents, is withdrawn from the cylinder.
- a solid fused mass of beryllium chloride adheres very tightly tothe sheet iron of the liner but it can be removed by hammering the sides of the liner.
- the material so recovered is completely solid, and relatively hard and dense.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Aprifi 8, N42 H. 's. COOPER 2,283,235
PROCESS OF FUSING OF BERYLLIUM CHLORIDE Filed Nov. 28, 1940 INVENTOR Hum: SLooPER Patented Apr. 28, 1942 2,281,235 I PROCESS OF'FUSING BERYLLIUM CHLORIDE Hugh S. Cooper, New York, N. IL, assign'or to Cooper-Wilford Beryllium, Ltd, Philadelphia, Pa., a corporation of Delaware 1 Application November 28, 1940, Serial No. 367,623
1 Claim.
This invention relates to the production of fused beryllium chloride.
An object of this invention is to make a form of anhydrous beryllium chloride that is less reactive with the atmosphere than has been possible with the formation of beryllium chloride according to the prior art.
Another object is to effect a fused form of beryllium chloride.
Still another object is to produce a form of beryllium chloride particularly effective for easy and economical production of berylliumthenefrom.
Other objects and advantages will be apparent from the following specification.
The drawing represents an illustrative diagrammatic section of the apparatus with which the method of this invention is practised.
In the manufacture of pure beryllium metal the common method is the electrolysis of anhydrous beryllium chloride in a suitable fused salt bath. For this and other purposes'the anhydrous chloride is made by the chlorination of the oxide or other oxy-compound of beryllium, usually at a temperature between 800 C. and 1000 C.
Since the vaporization temperature of the chloride is far below its temperature of formation in the chlorinator, it is of necessity-recovered by condensation. This produces a light, flufiy, and highly porous mass of thin needle crystals. In this form the chloride is extremely reactive with the atmosphere and can be stored for only a short time without deterioration, and only then by the exercise of extreme precautions and care. The use of this chloride of the prior art in an electrolytic bath for the making of beryllium is also a matter of considerable difiiculty. When it is added to the bath it tends to float on the surface where it vaporizes and oxidizes instead of going quickly into solution. The part These and other dimculties of the storage and use of beryllium chloride are overcome by its use in massive fused form. Since beryllium chloride vaporizes directly from the solid however, and
veniently be made of steel. The cylinder l is permanently closed at the bottom end. At its top the cylinder has a removable cap 2 held tightly in place by any convenient means, as for instance, the bolts 3 and the flange l. Drilled through the cap 2 is a hole 5 into which is screwed a short piece of pipe t. At its other end the pipe 6, carries a valve 1, which in turn communicates with a shortpiece of pipe 8, used to carry away efiluent gases. If desired the valve I may be an automatic check valve preventing gases from travelling inward toward the cylinder.
Inside the cylinder i is a liner f9-which can conveniently be made of sheet iron or the like. This liner also comprises a cylinder closed at the bottom only. This liner fits loosely into'the cylinder l with its bottom resting on the bottom of the cylinder. The liner 9 is filled with the ordinary fiuiiy beryllium chloride 90, in the'iorm in which it comes from the chlorinator. This chloride is tamped in place to increase the content as much as is conveniently possible.
Aiter the liner has been filled and placed in the cylinder, the cap 2 is securely fastened in place. The whole assembly is then placed in any suitable furnace such as is describedbelow and After a little while when the interior of the its liquid phase and is not easily obtainable under ordinary conditions, the melting of it is not normally either a simple or an easy procedure,
\ but it is rendered both simple and easy by means say, for gas or oil having flame projection it as will be clear.
Heat is now applied to the furnace and at the same time thevalve l is opened Just a crack.
cylinder has reached a temperature of about 100 0., fumes will start to be emitted from the point the valve 1 may be closed tightly without risk of building up any dangerous pressure in the cy inde The at g s continu d for a time longer, to make sure that all parts of the cylinder have reached a temperature of about 400 0., but without greatly exceeding that temperature. The valve 1 is tightly closed before the furnace is opened, in any case. and-certainly before any drop in temperature is permitted internally of the cylinder i. t
The cylinder is now removed from the furnace and permitted to cool. The cap 2 is then removed and'the liner 9, with its contents, is withdrawn from the cylinder. In the bottom of the liner is found a solid fused mass of beryllium chloride. It adheres very tightly tothe sheet iron of the liner but it can be removed by hammering the sides of the liner. The material so recovered is completely solid, and relatively hard and dense.
menses In the atmosphere it deteriorates only very slowly, particularly if it is kept in the form oi lumps. When it is added to a fused electrolytic bath it dissolves very rapidly with negligible vaporization. frothing, or oxidation, and results in larger electrolytic yields of metal.
Having described my invention the claim is as follows: i The process of fusing beryllium chloride which comprises heating it in a closed vessel to a temperature of about 300 C. while permitting the generated vapors to escape, and thereafter heating to a temperature of about 400 C. while keeping the vessel tightly closed.
HUGH S. COOPER.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US367623A US2281235A (en) | 1940-11-28 | 1940-11-28 | Process of fusing beryllium chloride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US367623A US2281235A (en) | 1940-11-28 | 1940-11-28 | Process of fusing beryllium chloride |
Publications (1)
Publication Number | Publication Date |
---|---|
US2281235A true US2281235A (en) | 1942-04-28 |
Family
ID=23447935
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US367623A Expired - Lifetime US2281235A (en) | 1940-11-28 | 1940-11-28 | Process of fusing beryllium chloride |
Country Status (1)
Country | Link |
---|---|
US (1) | US2281235A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2447210A (en) * | 1943-05-28 | 1948-08-17 | Edna W Roberts | Erythemal phosphor |
US4355227A (en) * | 1978-05-08 | 1982-10-19 | Seb S.A. | Apparatus for the destruction of microfiches and the like |
-
1940
- 1940-11-28 US US367623A patent/US2281235A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2447210A (en) * | 1943-05-28 | 1948-08-17 | Edna W Roberts | Erythemal phosphor |
US4355227A (en) * | 1978-05-08 | 1982-10-19 | Seb S.A. | Apparatus for the destruction of microfiches and the like |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2281235A (en) | Process of fusing beryllium chloride | |
US2754347A (en) | Apparatus for refining rare refractory metals | |
US2615706A (en) | Distillation of metals | |
US2780541A (en) | Process for treating molten metals | |
US2858189A (en) | Production of titanium tetrachloride | |
GB363954A (en) | Improvements in and relating to methods of coating metals | |
US1594345A (en) | Production of magnesium | |
US2368339A (en) | Process for producing aluminum brasses | |
US623693A (en) | Process of and apparatus for making caustic alkalies | |
US778270A (en) | Production of metallic magnesium. | |
US3318688A (en) | Process of producing zirconium metal | |
US2262164A (en) | Method for recovery of cadmium | |
US2256481A (en) | Producing flat-set copper shapes | |
US1403349A (en) | Method and means for refining metals | |
US1711738A (en) | Process for the direct reduction of iron from its ores | |
US1665844A (en) | Method of purifying metals | |
US1099451A (en) | Process for the continuous production of dry hydrochloric acid and potassium bisulfate from potassium chlorid and sulfuric acid. | |
US1043154A (en) | Electrolytic production of light metals. | |
US2812240A (en) | Process of making boron nitride | |
US2375199A (en) | Purification of metals | |
US1924648A (en) | Preformed abrasive and process of producing the same | |
US2276239A (en) | Method of treating magnesium | |
US1645144A (en) | Apparatus for purifying and solidifying aluminum chloride | |
US1533911A (en) | Electrolytic production of magnesium | |
US605379A (en) | Retort and method of making same |