US2274237A - Process for the removal of metallic magnesium from mixtures of beryllium and magnesium - Google Patents
Process for the removal of metallic magnesium from mixtures of beryllium and magnesium Download PDFInfo
- Publication number
- US2274237A US2274237A US340366A US34036640A US2274237A US 2274237 A US2274237 A US 2274237A US 340366 A US340366 A US 340366A US 34036640 A US34036640 A US 34036640A US 2274237 A US2274237 A US 2274237A
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- United States
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- beryllium
- magnesium
- metallic
- mixtures
- removal
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- Expired - Lifetime
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B35/00—Obtaining beryllium
Definitions
- magnesium is used in' a small excess. both metalsdo not or at any rate only slightly alloy with each other, a beryllium metal con- Patented 24, 1942 PROCESS FOR. TnEREMovAL oF M Er'ALLIo MAGNESIUMFROM MIXTURES OFBERYL. LIUM AND MAGNESIUM y Gustav Jaeger,,Neu-Isenburg,' and Alfred'Rudert,
- the contaminated beryllium metal may be .treated with aqueous solutions of definite a'cids.- Magnesium as well as the other metallic impurities may be removed in a simple manner-from the beryllium without difficulty and with a nearly imperceptible loss of metallic beryllium through a treatment with acetic acid, tartaric acid, citric acid and especially with nitric acid.
- the beryllium is preferably ground and poured over with one of the above mentioned acids or the beryllium is added under stirring at room temperature to one of these acids, whereby care is to be taken that the temperature does not exceed 60 C. in order to avoid a substantial attack on the beryllium. It has proved advantageous to keep the temperature between 10 and C. After finishing of the gas evolution, the beryllium is separated from the acid and-then washed. Temperature and period of influence depend on the composition of the mixture as well as. on the grade of distributionxof the single components.
- the concentration of the acid may vary in wide ranges.
- An-acid concentration of, for in stance, 0.5 to 1% nitric acid is already capable of Wholly separating the magnesium and other metallic impurities from the beryllium, during a period of several minutes only.
- Example 1 g. cuttings of beryllium with a content of 4.5% magnesium, 0.8% iron, 1.2% aluminium, 0.7% beryllium oxide are added at ordinary temperature to 300 cc. of a 3% nitric acid; the suspension is cooled and stirred to keep the temperature below 30C. After a period of 10 minutes the gas evolution has finished. The beryllium is filtered off and rinsed with water. The beryllium obtained was practically free from magnesium and other impurities, with a loss of V 1.7% beryllium.
- Example 2 100 g. beryllium powder with acontent of 6.5% magnesium, 0.5% nickel, 1.2% iron, 0.6% beryllium oxide were added under stirring and cooling to 300 cc.
- metallic impurities which comprises treating the impure beryllium in subdivided form with dilute nitric acid at a temperature between 10 C. and 30 C. r
- a process for the purification of impure beryllium containing magnesium as well as other metallic impurities which comprises treating the impure beryllium in'subdivided form with a 5% to 3% nitric acid at a temperature between 10 C.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
I beryllium and magnesium.
, ably magnesium is used in' a small excess. both metalsdo not or at any rate only slightly alloy with each other, a beryllium metal con- Patented 24, 1942 PROCESS FOR. TnEREMovAL oF M Er'ALLIo MAGNESIUMFROM MIXTURES OFBERYL. LIUM AND MAGNESIUM y Gustav Jaeger,,Neu-Isenburg,' and Alfred'Rudert,
Heilbronn,
Neckar, Germany,
assignors to Chemical Marketing Company Inc., New York, i
N. Y. t 1
No Drawing. Application June 13, 1940, Serial No. 340,366. In Germany May 27, 1939 3 Claims. (01. 75-421) Our invention relates to a process for removing metallic magnesium 'from' mixtures containing fAccording to the hithertoknown processes a really pure beryllium metal is noteasily to be obtained without observation of special precau-.
tions. Working upon a technical scale involves nearly always the occurrence of certain impuri ties in thefinal product although the process is carried out with utmost precaution. The quantities of these impurities are only small, however, in many fields of utilization an absolutely pure beryllium metal is obligatory.
It has beenknown to carry out the. process for, the recovery of metallic. beryllium by reducing certainsuitableberyllium compounds with metallic magnesium. Thus, for instance, beryllium chloride may be reacted with magnesium according to the formula To obtain a nearly complete reduction prefertaminated mainly with magnesium and to a lesser degree also with other metals is obtained.
It no pure beryllium chloride is available and the reaction carried out with a technical product, containing besidesmagnesium less electropositive elements, liberated by the reduction means such as, for instance, iron, manganese, aluminium, nickel or copper or the like, all these elements either alloyed or mechanically mixed will be found in the resulting metallic beryllium.
In addition to these'impurities all those coming from the vessel materials, such as'iron, copper, nickel or the like, or those occurring by the utilization, of not quite unattackable elec trodes such as tungsten or graphite, will also it be found in 'the metallic beryllium.
Obviously it is best to let all those impurities first pass into the final productand then to remove them in a onestep operation instead of trying to remove all the impurities through a quantity of suitable multi step operations.
According to our invention the contaminated beryllium metal may be .treated with aqueous solutions of definite a'cids.- Magnesium as well as the other metallic impurities may be removed in a simple manner-from the beryllium without difficulty and with a nearly imperceptible loss of metallic beryllium through a treatment with acetic acid, tartaric acid, citric acid and especially with nitric acid.
The fact that the solution contains'also berylliumatter dissolving of the impurities-may be explained in such manner that all crude beryllium contains certain quantities of oxide which also dissolve in the acids. The treatment'with acids, according to our invention, not only causes an improvement of beryllium with respect to its contamination with foreign metals but also in view to its contents of oxide, for instance, beryllium oxide and magnesium oxide or other metallic oxides occurring with the reduction of mag- 'nesium.
In carryingout our invention the beryllium is preferably ground and poured over with one of the above mentioned acids or the beryllium is added under stirring at room temperature to one of these acids, whereby care is to be taken that the temperature does not exceed 60 C. in order to avoid a substantial attack on the beryllium. It has proved advantageous to keep the temperature between 10 and C. After finishing of the gas evolution, the beryllium is separated from the acid and-then washed. Temperature and period of influence depend on the composition of the mixture as well as. on the grade of distributionxof the single components.
Very simple preliminary tests may easily ascertain the'bestworking conditions in every case.
The concentration of the acid may vary in wide ranges. An-acid concentration of, for in stance, 0.5 to 1% nitric acid is already capable of Wholly separating the magnesium and other metallic impurities from the beryllium, during a period of several minutes only.
Example 1 g. cuttings of beryllium with a content of 4.5% magnesium, 0.8% iron, 1.2% aluminium, 0.7% beryllium oxide are added at ordinary temperature to 300 cc. of a 3% nitric acid; the suspension is cooled and stirred to keep the temperature below 30C. After a period of 10 minutes the gas evolution has finished. The beryllium is filtered off and rinsed with water. The beryllium obtained was practically free from magnesium and other impurities, with a loss of V 1.7% beryllium. Example 2 100 g. beryllium powder with acontent of 6.5% magnesium, 0.5% nickel, 1.2% iron, 0.6% beryllium oxide were added under stirring and cooling to 300 cc. of a 10% acetic acid, at room'temperature. The gas evolution began immediately whereby the temperature did not rise over 25 C. Aftera period of 15 minutes the gas evolution had finished. fThe stirring was continued for an additional 5 minutes, then filtered off and thoroughly rinsed with water. A pure beryllium with a. loss of 2 .1% was obtained.
metallic impurities which comprises treating the impure beryllium in subdivided form with dilute nitric acid at a temperature between 10 C. and 30 C. r
3. A process for the purification of impure beryllium containing magnesium as well as other metallic impurities which comprises treating the impure beryllium in'subdivided form with a 5% to 3% nitric acid at a temperature between 10 C.
and 30 C.
GUSTAV JAEGER. ALFRED RUDERT.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2274237X | 1939-05-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
US2274237A true US2274237A (en) | 1942-02-24 |
Family
ID=7993331
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US340366A Expired - Lifetime US2274237A (en) | 1939-05-27 | 1940-06-13 | Process for the removal of metallic magnesium from mixtures of beryllium and magnesium |
Country Status (1)
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US (1) | US2274237A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2697660A (en) * | 1951-04-25 | 1954-12-21 | Merle E Sibert | Purification of titanium by washing and froth flotation |
US2847298A (en) * | 1954-07-02 | 1958-08-12 | Nat Res Corp | Method of producing refractory metals |
US2864690A (en) * | 1955-03-08 | 1958-12-16 | Nat Lead Co | Process for treating titanium metal |
US3930844A (en) * | 1975-02-06 | 1976-01-06 | The United States Of America As Represented By The Secretary Of The Navy | Method for disposal of pyrotechnic waste |
-
1940
- 1940-06-13 US US340366A patent/US2274237A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2697660A (en) * | 1951-04-25 | 1954-12-21 | Merle E Sibert | Purification of titanium by washing and froth flotation |
US2847298A (en) * | 1954-07-02 | 1958-08-12 | Nat Res Corp | Method of producing refractory metals |
US2864690A (en) * | 1955-03-08 | 1958-12-16 | Nat Lead Co | Process for treating titanium metal |
US3930844A (en) * | 1975-02-06 | 1976-01-06 | The United States Of America As Represented By The Secretary Of The Navy | Method for disposal of pyrotechnic waste |
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