US1925920A - Process for the preparation of oxide of beryllium - Google Patents
Process for the preparation of oxide of beryllium Download PDFInfo
- Publication number
- US1925920A US1925920A US641465A US64146532A US1925920A US 1925920 A US1925920 A US 1925920A US 641465 A US641465 A US 641465A US 64146532 A US64146532 A US 64146532A US 1925920 A US1925920 A US 1925920A
- Authority
- US
- United States
- Prior art keywords
- beryllium
- fluoride
- oxide
- solution
- alkali metal
- 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
- 229910052790 beryllium Inorganic materials 0.000 title description 29
- ATBAMAFKBVZNFJ-UHFFFAOYSA-N beryllium atom Chemical compound [Be] ATBAMAFKBVZNFJ-UHFFFAOYSA-N 0.000 title description 29
- 238000000034 method Methods 0.000 title description 10
- 238000002360 preparation method Methods 0.000 title description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 27
- 239000000243 solution Substances 0.000 description 15
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 11
- 229910052708 sodium Inorganic materials 0.000 description 11
- 239000011734 sodium Substances 0.000 description 11
- 239000003513 alkali Substances 0.000 description 9
- 238000001354 calcination Methods 0.000 description 9
- 229910052783 alkali metal Inorganic materials 0.000 description 7
- 150000001340 alkali metals Chemical class 0.000 description 7
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- 229910000288 alkali metal carbonate Inorganic materials 0.000 description 4
- 150000008041 alkali metal carbonates Chemical class 0.000 description 4
- LTPBRCUWZOMYOC-UHFFFAOYSA-N beryllium oxide Inorganic materials O=[Be] LTPBRCUWZOMYOC-UHFFFAOYSA-N 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 238000006467 substitution reaction Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 229910001515 alkali metal fluoride Inorganic materials 0.000 description 2
- 229910052614 beryl Inorganic materials 0.000 description 2
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- FRWYFWZENXDZMU-UHFFFAOYSA-N 2-iodoquinoline Chemical compound C1=CC=CC2=NC(I)=CC=C21 FRWYFWZENXDZMU-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical class F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 150000007514 bases Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- NJJFVOQXYCEZLO-UHFFFAOYSA-N dialuminum;triberyllium;dioxido(oxo)silane Chemical group [Be+2].[Be+2].[Be+2].[Al+3].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O NJJFVOQXYCEZLO-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000011872 intimate mixture Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
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
- C01F3/005—Fluorides or double fluorides of beryllium with alkali metals or ammonium; Preparation of beryllium compounds therefrom
-
- 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
- C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
- C22B26/20—Obtaining alkaline earth metals or magnesium
-
- 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
- the process according to the invention allows of obtaining the oxide of beryllium starting from a double fluoride of this metal and an alkali metal, by mixing intimately the double fluoride of beryllium and alkali metal with an alkali carbonate, calcining this mixture and afterwards washing it with hot water, in such a manner as to carry off the alkali metal from the double fluoride in the state of dissolved alkali fluoride and to convert the beryllium into the state of insoluble oxide, which is then sep arated out.
- This mixture is afterwards calcined for a suiiicient length of time in a crucible or upon an appropriate hearth made of magnesia or beryllium oxide for example, after which the roasted It is naturally advantageous to employ an excess of alkali carbonate, ten percent for instance, above that which is indicated by stechiometric relation between BeFz and NazCOs which is the only one to be considered.
- the double fluoride contains a slight excess of fluoride of beryllium or conversely that it corresponds to the formula BeFaZNaF.
- the temperature of calcination may cover a fairly wide range. It is good to operate between 525 and 550 C. One can go higher,- the practical limit being the point of fusion of the mixture, which it is advisable not to reach.
- the oxide of beryllium (BeO) obtained in the form of paste, as above described, is an industrial product which may retain still some hundredths of fluoride or" sodium according to the care taken in the washing operation.
- the yield of the process is remarkably high.
- This solution contains, except for working losses, the fluorine which was composed in the double fluoride of beryllium.
- the process comprises a large number of variations, in particular the substitution of a double fluoride of beryllium and potassium forthe double fluoride of beryllium and sodium, the substitution of carbonatev of potassium for the carbonate of sodium in the mixture destined for calcination, the substitution, for one or other of these carbonates, of
- an alkaline product capable of transforming 'it-' self into a basic compound by calcination such as an alkali oxalate or acetate, etc. etc.
- the whole solution is afterwards evapberyllium starting from a double fluoride of this metal and of an alkali metal, consisting in mixing intimately the double fluoride of beryllium and alkali metal with an alkali metal carbonate, calcining this mixture and washing it afterwards with hot water, thereby separating out the insoluble oxide of beryllium from the dissolved alkali metal fluoride.
- a process for the preparation of oxide of beryllium from a solution of a double fluoride of beryllium and of an alkali metal consisting in adding to said solution a small amount of an alkali metal carbonate adapted to precipitate the heavy metals present in said solution, separating the precipitate formed, adding the remaining necessary amount of the alkali metal carbonate to the purified solution of the double fluoride of beryllium and of an alkali metal, evaporating to dryness the whole solution, calcining the resulting mass, washing it afterwards with hot water, thereby separating out the insoluble oxide of beryllium from the dissolved alkali metal fluoride.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
Patented Sept. 5, 1933 i STATES PROCESS FOR THE PREPARATIQN OF OXIDE 0F BERYLLlillJll/I Robert Andre Gadeau, St. Jean E16 Maurienne, France, assignor to Compagnie dc Prodnits Chimiques et Electrometallurgiqnes Alais Froges et Carnalue, Paris, France, a corporation of France No Drawing. Application November 5,
Serial No. 641,465, and in France November 28,
3 Claims.
The preparation of oxide of beryllium (BeO) starting from natural beryl as theinitial primary material has hitherto required complicated operations.
The. best method of preliminary treatment 01 the beryl being at present that by the attack with fluosilicate of sodium at a temperature of about 650-700 0., from which there is with.- drawn by solution the double fiuoride or" beryllium and sodium, it is this last mentioned compound which serves as the point of departure for the present process.
It is known that the double fluoride of beryllium and of sodium, which is thus withdrawn from the solution derived from the. attacking oi beryl by fluosilicate of sodium, is a complex body in which the beryllium is linked to the sodium in a particularly strong manner, so that ammonia, which precipitates practically the whole of the beryllium in the state of hydrated oxide in the solutions of other salts oi beryllium (chloride, sulphate, nitrate), does not even separate the beryllium from the sodium when they are linked together by fluorine.
Neither do the alkaline hydroxides (NaOH and KOH), added in solution to the double fluoride or" beryllium and sodium, efiect a Satis factory precipitation of the beryllium in the state of hydroxide.
Much less has it been possible to obtain the separation of the element beryllium, in the same aqueous solution of this double fluoride, by means of the alkali carbonates (NazCOs or K2003) added in solution.
The process according to the invention allows of obtaining the oxide of beryllium starting from a double fluoride of this metal and an alkali metal, by mixing intimately the double fluoride of beryllium and alkali metal with an alkali carbonate, calcining this mixture and afterwards washing it with hot water, in such a manner as to carry off the alkali metal from the double fluoride in the state of dissolved alkali fluoride and to convert the beryllium into the state of insoluble oxide, which is then sep arated out.
One begins for instance with the complex fluoride BeFzNaF in a dry and finely pulverized state, with which one mixes intimately one molecular part of NazCOs in powder form.
This mixture is afterwards calcined for a suiiicient length of time in a crucible or upon an appropriate hearth made of magnesia or beryllium oxide for example, after which the roasted It is naturally advantageous to employ an excess of alkali carbonate, ten percent for instance, above that which is indicated by stechiometric relation between BeFz and NazCOs which is the only one to be considered.
it may in fact happen in practice that the double fluoride contains a slight excess of fluoride of beryllium or conversely that it corresponds to the formula BeFaZNaF.
In all cases, a beryllium test allows of determining the suitable proportion of NazCOs to be employed, as has just been stated.
The temperature of calcination may cover a fairly wide range. It is good to operate between 525 and 550 C. One can go higher,- the practical limit being the point of fusion of the mixture, which it is advisable not to reach.
The duration of the calcining operation depending on the mass brought under treatment, whilst it is reduced by the temperature and by the frequency of stirring, the state of progress and the end of the reaction are recognised by examination of a sample taken during the course of the operation.
The oxide of beryllium (BeO) obtained in the form of paste, as above described, is an industrial product which may retain still some hundredths of fluoride or" sodium according to the care taken in the washing operation.
The yield of the process is remarkably high.
By drying this paste at a stove temperature (120439 0.), one can obtain the BeO in powder, retaining a little water, and which dissolves, especially when hot, slowly in nitric acid, (but) rapidly and completely in hydrochloric and hydrofluoric acids.
With this oxide, thus obtained in the simplest and the most economical manner, one can with advantage prepare the fluoride of beryllium and the oxyfluoride, which are the most important 7 compounds for the production of metallic beryllium and its alloys, as Well as of other salts derived therefrom.
The fluoride of sodium which passes out from which in practice makes this solutionrconsist solely of alkali fluoride and thus capable of being utilized such as it is.
This solution contains, except for working losses, the fluorine which was composed in the double fluoride of beryllium.
It is well understood that the invention is not limited to the method of carrying it out such.
as described, and that the process comprises a large number of variations, in particular the substitution of a double fluoride of beryllium and potassium forthe double fluoride of beryllium and sodium, the substitution of carbonatev of potassium for the carbonate of sodium in the mixture destined for calcination, the substitution, for one or other of these carbonates, of
an alkaline product capable of transforming 'it-' self into a basic compound by calcination, such as an alkali oxalate or acetate, etc. etc.
One can also effect with advantage the intimate mixture of the double fluoride and of the alkali carbonate intended for calcination, when starting from the solution of the double fluoride, by operating in the following manner:
In the solution of the double fluoride, there is first added a small dose of alkali carbonate which produces the precipitation of the heavy metals, which may exist in small quantities; this precipitate is separated and into the solution of double fluoride thus purified, there is added the complement of alkali carbonate which corresponds to thecontent in fluoride of beryllium, according to the relationrpreviously indicated. The whole solution is afterwards evapberyllium starting from a double fluoride of this metal and of an alkali metal, consisting in mixing intimately the double fluoride of beryllium and alkali metal with an alkali metal carbonate, calcining this mixture and washing it afterwards with hot water, thereby separating out the insoluble oxide of beryllium from the dissolved alkali metal fluoride.
2. A process for the preparation of oxide of beryllium from a solution of a double fluoride of beryllium and of an alkali metal, consisting in adding to said solution a small amount of an alkali metal carbonate adapted to precipitate the heavy metals present in said solution, separating the precipitate formed, adding the remaining necessary amount of the alkali metal carbonate to the purified solution of the double fluoride of beryllium and of an alkali metal, evaporating to dryness the whole solution, calcining the resulting mass, washing it afterwards with hot water, thereby separating out the insoluble oxide of beryllium from the dissolved alkali metal fluoride. V
3. In the process according to claim 1, the provision consisting in substituting, for the alkali metal carbonate, a compound adapted to transform itself during the calcination into an equivalent reagent relatively to the double fluoride.
ROBERT ANDRE GADEAU.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1925920X | 1931-11-23 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1925920A true US1925920A (en) | 1933-09-05 |
Family
ID=9682294
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US641465A Expired - Lifetime US1925920A (en) | 1931-11-23 | 1932-11-05 | Process for the preparation of oxide of beryllium |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1925920A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5268334A (en) * | 1991-11-25 | 1993-12-07 | Brush Wellman, Inc. | Production of beryllium oxide powders with controlled morphology and quality |
-
1932
- 1932-11-05 US US641465A patent/US1925920A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5268334A (en) * | 1991-11-25 | 1993-12-07 | Brush Wellman, Inc. | Production of beryllium oxide powders with controlled morphology and quality |
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