US2281235A - Process of fusing beryllium chloride - Google Patents

Process of fusing beryllium chloride Download PDF

Info

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
Application number
US367623A
Inventor
Hugh S Cooper
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
COOPER WILFORD BERYLLIUM Ltd
COOPER-WILFORD BERYLLIUM Ltd
Original Assignee
COOPER WILFORD BERYLLIUM Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by COOPER WILFORD BERYLLIUM Ltd filed Critical COOPER WILFORD BERYLLIUM Ltd
Priority to US367623A priority Critical patent/US2281235A/en
Application granted granted Critical
Publication of US2281235A publication Critical patent/US2281235A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F3/00Compounds 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.
US367623A 1940-11-28 1940-11-28 Process of fusing beryllium chloride Expired - Lifetime US2281235A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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
US2022372A (en) Lead pot
US1981161A (en) Preparation of carbon disulphide and hydrogen sulphide
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
US778270A (en) Production of metallic magnesium.
US3318688A (en) Process of producing zirconium metal
US1467563A (en) Corrosion and heat resisting apparatus
US2256481A (en) Producing flat-set copper shapes
US1786202A (en) Apparatus for high-temperature treatment of ores and other substances
US1816742A (en) Method of producing tin
US2780539A (en) Process of smelting germanium
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.
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
US1555956A (en) Melting and pouring magnesium