US1704257A - Method of preparing refractory metals - Google Patents
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- US1704257A US1704257A US618544A US61854423A US1704257A US 1704257 A US1704257 A US 1704257A US 618544 A US618544 A US 618544A US 61854423 A US61854423 A US 61854423A US 1704257 A US1704257 A US 1704257A
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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
- C22B60/00—Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
- C22B60/02—Obtaining thorium, uranium, or other actinides
- C22B60/0291—Obtaining thorium, uranium, or other actinides obtaining thorium
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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
- C22B34/00—Obtaining refractory metals
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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
- C22B5/00—General methods of reducing to metals
- C22B5/02—Dry methods smelting of sulfides or formation of mattes
- C22B5/04—Dry methods smelting of sulfides or formation of mattes by aluminium, other metals or silicon
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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
- C22B60/00—Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
- C22B60/02—Obtaining thorium, uranium, or other actinides
- C22B60/0204—Obtaining thorium, uranium, or other actinides obtaining uranium
- C22B60/0213—Obtaining thorium, uranium, or other actinides obtaining uranium by dry processes
Definitions
- This invention relates to methods of obtainin'g metals from their compounds and more particularly from the diiiicultly reducible oxides of the rare refractory metals such as uranium, thorium, and the like.
- An object of the present invention is the provision of a process for the product1on of metals in a high state of purity.
- a further object of the invention is the provision of a process which may be controlled to obtain metal powders, particularly the rare refractory metal powders, in varying degrees of fineness.
- a further object of the invention is to provide a bomb in which chemical and metallurgical operations may be practiced without the introduction of impurities from the bomb into the products produced therein.
- a further object of the invention is to provide a process for protecting the products of the reaction from becoming contaminated by impurities introduced by the container in which the process is practiced.
- a still further object is to provide a method of lining a bomb in an expeditious and simple manner.
- the calcium method is open'to 0bjection because of the relative expensiveness of that metal and the impurities contained in the commercial material, also because the heat of reaction is high which causes coarseness of the powders through the agglomerations of the particles thereof.
- alkaline earth metal preferably calcium
- fluxin agent a halide of the same alkaline cart I metal being inabout 50% excess of the theoretical quantity required.
- This mixture is heated in a suitable vessel, preferably a bomb, which is evacuated or provided with any other suitable inert environment from which nitrogen and oxygen are absent.
- the bomb comprises a hollow iron cylinder 2 having a chamber 3 within the same.
- the bomb may be about 10 inches in height and 4 inches in diameter with a wall thickness of approximately a half inch.
- the upper end 4 of the bomb is provided with an internal tapered thread 5 'into which fits a tapered threaded plug 6 to the threads of which a sealing compound may be applied just previous to the insertion of the plug into the bomb.
- the inner walls of the chamber 3 in the bomb are referably provided with an insulating layer of calcium oxide or other satisfactory material which may preferably be applied in a manner more fully described hereinafter.
- the contents thereof may be removed by means of a star drill which is small enough so'that it does not touch the sides of the'bomb at any time and which has a stop on the handle so that the drill cannot come closer than of the bottom. In that way practically all of the charge is removed, but no iron is knocked loose from the bomb mechanically and practically no corrosion can take place or iron be introduced since there is no contact between thespecimen and the metal of the bomb.
- the contents of the bomb upon removal may be treated in any' well known manner to remove the undesirable products of the reaction.
- purification may consist of washing with dilute acid, water, etc. so that only the pure metal powder remains.
- the alkaline earth metal halide may, with certain refractory oxides,'serve as a flux so that the oxide is converted to the chloride, partially at least, where it is readily reduced.
- the pow der which is formed usually settles to the bottom of the fused mass so that the fluid calcium chloride would very effectually seal it away if any leakage in the bomb occurred after the reduction of the metal.
- the calcium chloride serves as a medium so that the calcium and the oxide come very intimately into contact. Thereduction, therefore, .by this method, is very complete.
- the alkaline earth metal halide or flux material slows up the reduction and thus provides a means for the regulation of the coarseness of the powder by the excess of the fluxing agent, so that when the temperature of reduction and the excess of reducing agent are once determined, a practically 100% yield of the metal powder may be obtained without losing any large amount of it, which would necessarily have to'be screened away on account of it being too coarse to press.
- the temperature and amount of fiux material may be regulated within certain limits so that successive preparations of the powder give uniform results. I y
- uranium oxide as an example of a diflicultly reducible oxide
- calcium as the alkaline earth metal or reducing agent
- calcium chloride as the alkaline earth halide or fluxing agent
- An intimate mixture is prepared in any suitable manner of 92 parts by weight of uranium oxide (U 0 or under slightly differing conditions equivalent quantities of the other oxides of uranium, a large excess (120 parts by weight) of calcium prepared from purifier calcium chloride, and a suitable uantity or about 200 parts by weight of purifled calcium chloride.
- the calcium chloride purchased as chemically pure and labelled calcined contains water, and in practicing our process we prefer to carefully dry the same at about 450 C. or at a higher temperature, so that it contains only a few tenths of one percent of moisture. If the commercial calcined calcium chloride is used, then it is necessary to employ an excess of calcium to combine with the oxygen. It is desirable to have very pure materials, since a small amount of iron for example, appears to cause beading due to the formation of low-melting point alloys, etc. Silicon also makes the metal hard and brittle:
- the mixture is pressed into cakes somewhat smaller than the bomb into which they are placed.
- a lining of pure calcium oxide is placed around the cakes in the manner heretofore described, after which the bomb is sealed.
- the bomb may then be evacuated or provided with an inert environment, or in lieu of this treatment a lump of calcium may be placed on top of the charge, prior to sealin g o l the bomb, tocombine with any residual air remaining within the same.
- External heat is applied to raise the temperature of the bomb to a bright red heat or about 900 C. to 1000 C. and this temperature is maintained from two to three hours.
- the temperature limit to which the'bomb is heated depends upon the actual proportion of calcium and calcium chloride used and upon the duration of heating.
- the powder is partially dried by suction and it is then quickly put through a 200 mesh screen a little at a time. If the powder is exposed to the air for a short time,'it frequently spontaneously ignites and is burned to oxide so that this must be done quickly.
- the powder is preserved by being'placed in pure alcohol.
- the lining material may be ressed around a core, which latter may be wit drawn, or it may be wetted and painted in.
- a core which latter may be wit drawn, or it may be wetted and painted in.
- other materials u i o o
- the mass is allowed to disinte rate 1n gen chloride, thus avoiding the use of water may be employed as the lining material, for example, strontium oxide.
- the material employed or the method followed in lining the bomb with the same should be such as to avoid the introduction of impurities.
- the method of producing rare refractory metals such. as uranium, thorium and the like from their diflicultly reducible oxides which comprises heating to a reacting temperature such oxides, an alkaline earth metal and an alkaline earth halide.
- the method of producing rare refractory metals such as uranium, thorium and the like from their difiicultly reducible oxides which comprises heating to a reacting temperature such oxides, an alkaline earth metal and an alkaline earth halide, the base of which is-the same as the alkaline earth metal employed.
- the method which comprises forming a mixture of uranium oxide, and alkaline earth halide and an alkaline metal, enclosing said mixture in a bomb, excluding oxygen and nitrogen from said bomb, raisin the mixture to reaction temperature, permitting the bomb to cool, and then treating the reaction pro'ducts to eliminate all except the uranium.
- the method of producing uranium powder of any degree of fineness which comprises forming a mixture of any uranium oxide such as U0 an alkaline earth halide and an alkaline earth metal, the proportions of the last named ingredient'being in about 50% excess of the theoretical quantity required, placing the mixture in 'a bomb, excluding oxy n and nitrogen from said bomb, heating the mb to a red heat for about two hours, permitting the bomb to cool and treating the reaction products to eliminate all but the uranium powder.
- the method of producing uranium powder of any degree of fineness which comprises heating to a reacting temperature an oxide of uranium, calcium and calcium chloride in predetermined excess proportionsand applying heat for a predetermined period depending upon the fineness of powder desired and the particular oxide of uranium used.
- the method of reducing diflicultly reducible oxides of refractory metals which comprises heating the oxide of a refractory metal in the presence of a halide to convert the oxide to a halide and simultaneously reducing the halide thus formed.
- the method of reducing the diflicultl reducible oxides of refractory metals whic comprises heating to a reacting temperature, an oxide of a refractory metal and an alkaline earth halide to convert the oxide to arefractory metal halide and simultaneously converting the halide to metal by means of cal- 0mm.
- the method of reducing the difiicultl reducible oxides of refractory metals whic comprises heating to a reacting temperature, an oxide of a refractory metal and calcium chloride to convert the oxide to refractor metal chloride, rendering inefi'ective such products of the reaction which prevent the reduction from going to completion and simultaneousl reducin the refractory metal halide thus ormed bylieating the same in the presence of calcium.
- the method of reducing the difiicultl reducible oxides of refractory metals whic comprises heating to a reacting temperature
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- Manufacturing & Machinery (AREA)
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- General Life Sciences & Earth Sciences (AREA)
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Description
March 1929. J. w. MARDEN ET m. 1,704,257
lmruon OF PREPARING REFRACTORY mum Original Filed Feb. 12, 1923 II I i i" I l/ VENTO J HN MARDEN THO/1 RTHOMAS JOHN E. CONLE v BY ATTORNEY JOHN WESLEY MARDEN, OI? EAST ORANGE, AND THOMAS PHILIP TH OMAS AND some EDWARD OONLEY, OF BLOOMFIELD, NEW JERSEY, ABBIGNOBB '10 WESTINGHOUSE LAMP COMPANY, A. CORPORATION OF PENNSYLVANIA.
METHOD OF PREPARING REFRACTORY METALS.
Application filed February 12, 1923, Serial No. 818,544. Renewed February 8, 1827.
This invention relates to methods of obtainin'g metals from their compounds and more particularly from the diiiicultly reducible oxides of the rare refractory metals such as uranium, thorium, and the like.
An object of the present invention is the provision of a process for the product1on of metals in a high state of purity.
A further object of the invention is the provision of a process which may be controlled to obtain metal powders, particularly the rare refractory metal powders, in varying degrees of fineness.
A further object of the invention is to provide a bomb in which chemical and metallurgical operations may be practiced without the introduction of impurities from the bomb into the products produced therein.
A further object of the invention is to provide a process for protecting the products of the reaction from becoming contaminated by impurities introduced by the container in which the process is practiced.
A still further object is to provide a method of lining a bomb in an expeditious and simple manner.
Other objects of the invention will be aparent from a reading of the following speci- Ecation.
It has been proposed to obtain the powders of metals, the oxides of which cannot be reduced to metal by means of hydrogen, for
example the oxides of uranium, zirconium, thorium, vanadium, tantalum, chromium, titanium, etc. or any other similarly difiiculty reducible oxide, by the well known metallurgical processes, one of which involved the reduction of the oxides by means of calcium as a reducing agent. Attemptshave also been made to reduce the oxides of certain of the metals mentioned by the alkali metals, but without success. The calcium method is open'to 0bjection because of the relative expensiveness of that metal and the impurities contained in the commercial material, also because the heat of reaction is high which causes coarseness of the powders through the agglomerations of the particles thereof.
In order to render effective the alkali metal reduction a further proposal has been made to employ an alkali metal as the reducing agent, together with a fluxing agent such as an alkaline earth halide or an alkali metal halide of a metal other than the alkali metal employed as the reducing agent. This method has been very successful, although open to several objections when it is the desire to obtain a very pure powder possessing a certain coarseness.
In practicing the methods referred to above, it has beenv custome to insert the mixed ingredients in an iron omb, and after sealing the latter, the reaction is started by heating the bomb. The iron, in some manner, finds its way into the metal produced, so that when the powder is sintered to reduce it to the coherent state, it forms, it is believed, with the iron, a low-melting point alloy which forms beads and runs out from the mass leaving cracks in the material and also causing a great deal of trouble in the furnace.
Attempts have been made to prevent the introduction of the iron impurity by lining the bomb with nickel, copper, chromium, etc., but in each case, metallic impurities were introduced ,which were most undesirable in preparing pure metals.
To illustrate the effect on the physical properties of a metal by the introduction of a small amount of an impurity, reference need only be made to the effect of carbon or any metallic impurity in pure iron. For example, .a small amount of silicon or carbon, when introduced into iron, causes the latter to become hard and brittle. The same effect will probably be produced if instead of iron, say uranium or thorium, were used. From our experience. with the rare refractory metals and their preparation, we are convinced that when iron is present as an impurity, it is very difficult to obtain the metal with which it is combined in a solid coherent condition owing to the beading previously referred to.
Therefore, in order to provide a process which may be practiced to obtain the rare refractory metal powders in avery pure state and of a predetermined degree offineness, the following method has been devised.
In practicing our invention we employ as the reducing agent an alkaline earth metal, preferably calcium, and employ as the fluxin agent a halide of the same alkaline cart I metal being inabout 50% excess of the theoretical quantity required. This mixture is heated in a suitable vessel, preferably a bomb, which is evacuated or provided with any other suitable inert environment from which nitrogen and oxygen are absent.
In the accompanying drawing 1s;1llustrated a vertical sectional view, partly in elevatipn,
of a bomb provided with an insulating hnmgof calcium oxide, within which the charge is placed. The bomb comprises a hollow iron cylinder 2 having a chamber 3 within the same. The bomb may be about 10 inches in height and 4 inches in diameter with a wall thickness of approximately a half inch. The upper end 4 of the bomb is provided with an internal tapered thread 5 'into which fits a tapered threaded plug 6 to the threads of which a sealing compound may be applied just previous to the insertion of the plug into the bomb. The inner walls of the chamber 3 in the bomb are referably provided with an insulating layer of calcium oxide or other satisfactory material which may preferably be applied in a manner more fully described hereinafter. I
In placing the mixture into the bomb, we observe the following precautions in order to prevent the introduction of impurities from the bomb. The bottom 8 of the bomb is covered with a layer 9 of pure, specially prepared highly ignited lime which contains no iron, silicon, or insoluble impurities. By insoluble impurities we mean insoluble in dilute acetic acid. After the bottom of the bomb has been covered about a quarterinch deep by thoroughly packing with a clean iron plunger, the mixture of calcium chloride, finely cut calcium, and the rare refractory metal oxide is pressed into cakes 11 somewhat smaller than the inside of the bomb. A cake is placed centrally on the lined bottom of the bomb and lime powder 12 is run in around the cake and packed down with a clean copper oriron ring. Usually,,three or four cakes are pressed and put in, one at a time, the lime being packed around each one of them after its introduction within the bomb, so that the final formation comprises an insulating layer of the lime interposed between the mixture and the walls of the bomb. A piece 13 of calcium is placed upon the uppermost cake to combine with the residual air remaining in the bomb or materials within the same. The bomb is then sealed by inserting the plug 6 after having previously applied a sealing mixture of magnesium oxide and linseed oil thereto. The bomb may be evacuated or provided with an inert environment, although we do not find this necessary as the lump of calcium removes the residual air. The reaction is then started by the external application of heat.
After the reaction is complete and the bomb permitted to cool, the contents thereof may be removed by means of a star drill which is small enough so'that it does not touch the sides of the'bomb at any time and which has a stop on the handle so that the drill cannot come closer than of the bottom. In that way practically all of the charge is removed, but no iron is knocked loose from the bomb mechanically and practically no corrosion can take place or iron be introduced since there is no contact between thespecimen and the metal of the bomb.
.We may also, if the bomb and the contents are kept cool, disintegrate the charge with water, which process avoids the necessity of 7 cutting loose the charge with a drill. In practicing this method of removal, considerable care should be exercised to have the bomb and contents cool, otherwise the rare metal powder, particularly in the case of uranium, will interact with the hot water and thus destroy the formers purity.
The contents of the bomb upon removal may be treated in any' well known manner to remove the undesirable products of the reaction. For example, such purification may consist of washing with dilute acid, water, etc. so that only the pure metal powder remains.
We believe that by practicing the foregoing method more nearly ideal conditions prevail for the production of pure metal powders for the following reasons: First, the alkaline earth metal halide may, with certain refractory oxides,'serve as a flux so that the oxide is converted to the chloride, partially at least, where it is readily reduced. Second, the pow der which is formed usually settles to the bottom of the fused mass so that the fluid calcium chloride would very effectually seal it away if any leakage in the bomb occurred after the reduction of the metal. Third, the calcium chloride serves as a medium so that the calcium and the oxide come very intimately into contact. Thereduction, therefore, .by this method, is very complete. Fourth, the alkaline earth metal halide or flux material slows up the reduction and thus provides a means for the regulation of the coarseness of the powder by the excess of the fluxing agent, so that when the temperature of reduction and the excess of reducing agent are once determined, a practically 100% yield of the metal powder may be obtained without losing any large amount of it, which would necessarily have to'be screened away on account of it being too coarse to press. By following the method outlined, we have found that the temperature and amount of fiux material may be regulated within certain limits so that successive preparations of the powder give uniform results. I y
In applicants copending application, Serial No. 504,154, filed September 29, 1921, assigned to the present assignee, reference is purpose.
To enable those skilled in the art to practice our invention, we will describe, in detail,
one method of applying the principle in-' volved, and, for this purpose, will select uranium oxide as an example of a diflicultly reducible oxide, calcium as the alkaline earth metal or reducing agent, and calcium chloride as the alkaline earth halide or fluxing agent.
An intimate mixture is prepared in any suitable manner of 92 parts by weight of uranium oxide (U 0 or under slightly differing conditions equivalent quantities of the other oxides of uranium, a large excess (120 parts by weight) of calcium prepared from purifier calcium chloride, and a suitable uantity or about 200 parts by weight of purifled calcium chloride. The calcium chloride purchased as chemically pure and labelled calcined contains water, and in practicing our process we prefer to carefully dry the same at about 450 C. or at a higher temperature, so that it contains only a few tenths of one percent of moisture. If the commercial calcined calcium chloride is used, then it is necessary to employ an excess of calcium to combine with the oxygen. It is desirable to have very pure materials, since a small amount of iron for example, appears to cause beading due to the formation of low-melting point alloys, etc. Silicon also makes the metal hard and brittle:
The mixture is pressed into cakes somewhat smaller than the bomb into which they are placed. A lining of pure calcium oxide is placed around the cakes in the manner heretofore described, after which the bomb is sealed. The bomb may then be evacuated or provided with an inert environment, or in lieu of this treatment a lump of calcium may be placed on top of the charge, prior to sealin g o l the bomb, tocombine with any residual air remaining within the same. External heat is applied to raise the temperature of the bomb to a bright red heat or about 900 C. to 1000 C. and this temperature is maintained from two to three hours. The temperature limit to which the'bomb is heated depends upon the actual proportion of calcium and calcium chloride used and upon the duration of heating. Definite instructions concerning this matter are not given for the reason the proportions and duration of heating must be varied with different grade oxides, which are used. For example, uranium oxide having the chemical formula U0 takes a different temperature, excess of reagents and time of heating than is required for the oxide having the formula U 0 After the completion of the reaction, the products are allowed to cool and are then removed from the container by means of a drill or the charge is simply disintegrated with water as above indicated. The mass is treated in any desired manner well known to one skilled in the art to eliminate all but the uranium owder.
The fol owing procedure has been followed in treatin the products of the reaction to remove all but the rare refractory metal powder. water, the latter being constantly stirred so as to bring about a more intimate contact with the mass. After settling, the supernatant liquor is decanted, and the residue washed with fresh water. The washing treatment is. repeated several times after which dilute acetic acid is added to the residue to remove matter soluble therein. The residue is then washed with water and the residue again acidified as before. The acid and water washing treatments are repeated about four times after which the residue is put through a. suction filter and washed with distilled water. The distilled water washing in the filter is followed by washing with alcohol. The powder is partially dried by suction and it is then quickly put through a 200 mesh screen a little at a time. If the powder is exposed to the air for a short time,'it frequently spontaneously ignites and is burned to oxide so that this must be done quickly. The powder is preserved by being'placed in pure alcohol. Before forming the powder into a slug for treatment in accordance with the metallurgical process described in the application of John W. Marden and H. C. Rentschler, Serial No. 432,325, filed December 21, 1920, and assigned to the Westinghouse Lamp Company, it is given the acid-wash treatment described in the application of John W. Marden, Serial No. 583,376, filed August 21, 1922, and assigned to the Westinghouse Lamp Compan T e powder thus produced readily passes the 200 mesh sieve and can be pressed into hard solid cakes having much the appearance of molybdenum under the same conditions. It might be stated that when the powder is too fine it can be filtered only with difficulty and when pressed squeezes out at the sides of the press. When the powder is too fine,it is extremely difficult todegasify in the furnace since t e large volume of gas causes cracks to be produced even when extreme care is exercised. It is usually necessary to press and handle pure uranium powder wet with alcohol in order to avoid spontaneous combustion in the air. Also a powder which is too fine shrinks to a large extent in the furnace. yielding misshapen slugs or buttons. 1 When a powder is too coarse it does not hold itsshape after pressing, but crumbles and can be handled only with difficulty.
Many other methods may be followed in lining the bomb. For instance, the lining material may be ressed around a core, which latter may be wit drawn, or it may be wetted and painted in. Obviously other materials u i o o The mass is allowed to disinte rate 1n gen chloride, thus avoiding the use of water may be employed as the lining material, for example, strontium oxide. owever, it should be remembered that the material employed or the method followed in lining the bomb with the same should be such as to avoid the introduction of impurities.
If so desired, when calcium and calcium chloride are used as reducing agents, it is possible to completely remove the undesirable products of the reaction and the excess of reducing agents by means of pure alcohol and a solution of an acid in alcohol such as hydroand contamination due thereto.
In practicing our process we emphasize the im 'ortance of em loying pure materials in or er to obtain tlie pure refractory metal powders. Therefore, such precautionary measures may be taken, as practice may dictate, of eliminating, as far as is practically possible, from the materials, such as the oxides, the calcium, the calcium chloride, the calcium oxide, and other reagents, any impurities, such as iron, free carbon, carbides, etc., which ma be present therein and which may operate etrimentally in reducing the refractory metal powder to the homogeneous coherent condition by heat treatment in the vacuum furnace described in the copending application of Harvey C. Rentschler, Serial Number 430,118 filed December 13, 1920, and assigned to the Westinghouse Lamp Company.
Modifications of the process described above may occur to those skilled in the art, but such as fall within the scope of the appended claims are contemplated by us as forming part of our invention."
What is claimed is:
1. The method of producing rare refractory metals such. as uranium, thorium and the like from their diflicultly reducible oxides which comprises heating to a reacting temperature such oxides, an alkaline earth metal and an alkaline earth halide.
"2. The method of producing rare refractory metals such as uranium, thorium and the like from their difiicultly reducible oxides which comprises heating to a reacting temperature such oxides, an alkaline earth metal and an alkaline earth halide, the base of which is-the same as the alkaline earth metal employed.
and calcium.
6. The method which comprises forming a mixture of uranium oxide, and alkaline earth halide and an alkaline metal, enclosing said mixture in a bomb, excluding oxygen and nitrogen from said bomb, raisin the mixture to reaction temperature, permitting the bomb to cool, and then treating the reaction pro'ducts to eliminate all except the uranium.
7 The method of producing uranium powder of any degree of fineness which comprises forming a mixture of any uranium oxide such as U0 an alkaline earth halide and an alkaline earth metal, the proportions of the last named ingredient'being in about 50% excess of the theoretical quantity required, placing the mixture in 'a bomb, excluding oxy n and nitrogen from said bomb, heating the mb to a red heat for about two hours, permitting the bomb to cool and treating the reaction products to eliminate all but the uranium powder.
8. The method of producing uranium powder of any degree of fineness which comprises heating to a reacting temperature an oxide of uranium, calcium and calcium chloride in predetermined excess proportionsand applying heat for a predetermined period depending upon the fineness of powder desired and the particular oxide of uranium used.
9. The method of reducing diflicultly reducible oxides of refractory metals which comprises heating the oxide of a refractory metal in the presence of a halide to convert the oxide to a halide and simultaneously reducing the halide thus formed.
I 10. The method of reducing the diflicultl reducible oxides of refractory metals whic comprises heating to a reacting temperature, an oxide of a refractory metal and an alkaline earth halide to convert the oxide to arefractory metal halide and simultaneously converting the halide to metal by means of cal- 0mm.
11. The method of reducing the difiicultl reducible oxides of refractory metals whic comprises heating to a reacting temperature, an oxide of a refractory metal and calcium chloride to convert the oxide to refractor metal chloride, rendering inefi'ective such products of the reaction which prevent the reduction from going to completion and simultaneousl reducin the refractory metal halide thus ormed bylieating the same in the presence of calcium.
12. The method of reducing the difiicultl reducible oxides of refractory metals whic comprises heating to a reacting temperature,
an oxide of the refractory metal, a converting agent capable of converting the oxide to a halide and also capable of removing reaction products which retard further conversion, and a reducing agent capable of reducuranium powder by reduction of an oxide ing said refractory metal halide which is thereof inabomb, which consists in surroundformed during the reaction. ing the charge with an insulating layer of 13. The step in the production of pure rare calcium oxide.
5 refractory metal powders by reduction of the In testimony whereof, we have hereunto oxides in a bomb which consists in insulating subscribed our names this 10th day of Febthe charge from the walls of the bomb by ruary,1923. interposing a layer of calcium oxide between JOHN WESLEY MARDE'N. the charge and, the walls of the bomb. THOMAS PHILIP THOMAS.
10 14. The step in the production of pure JOHN EDWARD CONLEY.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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US618544A US1704257A (en) | 1923-02-12 | 1923-02-12 | Method of preparing refractory metals |
GB16275/24A GB238663A (en) | 1923-02-12 | 1924-07-07 | Improvements relating to extraction of metals from their compounds |
CH111823D CH111823A (en) | 1923-02-12 | 1924-08-05 | Process for obtaining metals with a high melting point starting from their oxides. |
FR584599D FR584599A (en) | 1923-02-12 | 1924-08-12 | Improvements in methods of extracting metals from their compounds |
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US618544A US1704257A (en) | 1923-02-12 | 1923-02-12 | Method of preparing refractory metals |
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US1704257A true US1704257A (en) | 1929-03-05 |
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US618544A Expired - Lifetime US1704257A (en) | 1923-02-12 | 1923-02-12 | Method of preparing refractory metals |
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US (1) | US1704257A (en) |
CH (1) | CH111823A (en) |
FR (1) | FR584599A (en) |
GB (1) | GB238663A (en) |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2446062A (en) * | 1945-01-23 | 1948-07-27 | Westinghouse Electric Corp | Manufacture of thorium |
US2537068A (en) * | 1946-11-26 | 1951-01-09 | Westinghouse Electric Corp | Manufacture of zirconium |
US2727817A (en) * | 1953-09-23 | 1955-12-20 | Ethyl Corp | Method of producing titanium and recovering sodium |
US2777763A (en) * | 1955-09-14 | 1957-01-15 | Ethyl Corp | Method of producing titanium |
US2785064A (en) * | 1944-12-08 | 1957-03-12 | Harley A Wilhelm | Method of forming crucibles and reaction chambers for production of uranium of high purity |
US2794732A (en) * | 1954-05-03 | 1957-06-04 | Metal Hydrides Inc | Method for preparing calcium |
US2794733A (en) * | 1954-05-03 | 1957-06-04 | Metal Hydrides Inc | Method for preparing calcium |
US2801915A (en) * | 1952-03-18 | 1957-08-06 | Union Carbide Corp | Reduction of metal compounds in the presence of sulphur |
US2830894A (en) * | 1947-11-07 | 1958-04-15 | Frank H Spedding | Production of uranium |
US2834667A (en) * | 1954-11-10 | 1958-05-13 | Dominion Magnesium Ltd | Method of thermally reducing titanium oxide |
US2850379A (en) * | 1954-03-15 | 1958-09-02 | Ethyl Corp | Process for production of refractory metals |
US2886429A (en) * | 1943-10-07 | 1959-05-12 | William H Cooke | Method for the reduction of uranium compounds |
US2890110A (en) * | 1950-05-10 | 1959-06-09 | Richard D Baker | Production of plutonium from plutonium fluoride |
US2906618A (en) * | 1944-02-18 | 1959-09-29 | Crawford John William Croom | Process for production of uranium |
US3031413A (en) * | 1959-09-29 | 1962-04-24 | American Cyanamid Co | Solution of a carbide in a molten halide |
US3091526A (en) * | 1957-01-08 | 1963-05-28 | Union Carbide Corp | High-purity titanium production |
US3369889A (en) * | 1967-07-06 | 1968-02-20 | Atomic Energy Commission Usa | Production of spheroidal uranium metal powder |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1029166B (en) * | 1952-10-04 | 1958-04-30 | Helmut V Zeppelin Dr Ing | Process for the production of titanium, zirconium and other difficult-to-melt metals |
US2926082A (en) * | 1956-11-27 | 1960-02-23 | Ethyl Corp | Production of thorium |
FR2052082A5 (en) * | 1969-07-11 | 1971-04-09 | Commissariat Energie Atomique | |
BR8402087A (en) * | 1984-05-04 | 1985-12-10 | Vale Do Rio Doce Co | PROCESS OF OBTAINING METALLIC TITANIUM FROM ANASTASIA CONCENTRATE, BY ALUMINOTERMIA AND MAGNESIOTERMIA |
DE3817553A1 (en) * | 1988-05-24 | 1989-11-30 | Leybold Ag | METHOD FOR PRODUCING TITANIUM AND ZIRCONIUM |
EP1512475B1 (en) * | 2002-06-13 | 2009-09-23 | The Foundation for the Promotion of Industrial Science | Method for producing metal powder and formed product of raw material for metal |
-
1923
- 1923-02-12 US US618544A patent/US1704257A/en not_active Expired - Lifetime
-
1924
- 1924-07-07 GB GB16275/24A patent/GB238663A/en not_active Expired
- 1924-08-05 CH CH111823D patent/CH111823A/en unknown
- 1924-08-12 FR FR584599D patent/FR584599A/en not_active Expired
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2886429A (en) * | 1943-10-07 | 1959-05-12 | William H Cooke | Method for the reduction of uranium compounds |
US2906618A (en) * | 1944-02-18 | 1959-09-29 | Crawford John William Croom | Process for production of uranium |
US2785064A (en) * | 1944-12-08 | 1957-03-12 | Harley A Wilhelm | Method of forming crucibles and reaction chambers for production of uranium of high purity |
US2446062A (en) * | 1945-01-23 | 1948-07-27 | Westinghouse Electric Corp | Manufacture of thorium |
US2537068A (en) * | 1946-11-26 | 1951-01-09 | Westinghouse Electric Corp | Manufacture of zirconium |
US2830894A (en) * | 1947-11-07 | 1958-04-15 | Frank H Spedding | Production of uranium |
US2890110A (en) * | 1950-05-10 | 1959-06-09 | Richard D Baker | Production of plutonium from plutonium fluoride |
US2801915A (en) * | 1952-03-18 | 1957-08-06 | Union Carbide Corp | Reduction of metal compounds in the presence of sulphur |
US2727817A (en) * | 1953-09-23 | 1955-12-20 | Ethyl Corp | Method of producing titanium and recovering sodium |
US2850379A (en) * | 1954-03-15 | 1958-09-02 | Ethyl Corp | Process for production of refractory metals |
US2794733A (en) * | 1954-05-03 | 1957-06-04 | Metal Hydrides Inc | Method for preparing calcium |
US2794732A (en) * | 1954-05-03 | 1957-06-04 | Metal Hydrides Inc | Method for preparing calcium |
US2834667A (en) * | 1954-11-10 | 1958-05-13 | Dominion Magnesium Ltd | Method of thermally reducing titanium oxide |
US2777763A (en) * | 1955-09-14 | 1957-01-15 | Ethyl Corp | Method of producing titanium |
US3091526A (en) * | 1957-01-08 | 1963-05-28 | Union Carbide Corp | High-purity titanium production |
US3031413A (en) * | 1959-09-29 | 1962-04-24 | American Cyanamid Co | Solution of a carbide in a molten halide |
US3369889A (en) * | 1967-07-06 | 1968-02-20 | Atomic Energy Commission Usa | Production of spheroidal uranium metal powder |
Also Published As
Publication number | Publication date |
---|---|
GB238663A (en) | 1925-08-27 |
CH111823A (en) | 1925-09-16 |
FR584599A (en) | 1925-02-10 |
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