US2905551A - Manufacturing of metallic uranium - Google Patents
Manufacturing of metallic uranium Download PDFInfo
- Publication number
- US2905551A US2905551A US554909A US55490955A US2905551A US 2905551 A US2905551 A US 2905551A US 554909 A US554909 A US 554909A US 55490955 A US55490955 A US 55490955A US 2905551 A US2905551 A US 2905551A
- Authority
- US
- United States
- Prior art keywords
- uranium
- silicon
- oxides
- approximately
- silicides
- 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
- 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
-
- 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
- C22B60/0208—Obtaining thorium, uranium, or other actinides obtaining uranium preliminary treatment of ores or scrap
-
- 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
- C22B60/0217—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes
- C22B60/0221—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes by leaching
- C22B60/0247—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes by leaching using basic solutions or liquors
Definitions
- This invention relates to a process for the manufacture of metallic uranium.
- the primary object of the present invention is to generally improve the manufacture of metallic uranium.
- a more specific object is to provide a process which will make it possible to reduce uranium oxides to metal without the roundabout Way over the halides.
- Other objects of this invention will appear from the following description.
- the objects are achieved by comminuting the starting uranium oxides, working the comminuted oxides with a reducing gelatinous preparation into a paste, thoroughly mixing the mass thus obtained with silicon powder, and compressing the mixture into one or more individual pieces.
- the compressed pieces are heated and subjected to a reducing action and yield a melt bearing uranium and silicon.
- the silicides in the melt are converted by a thermal aftertreatment into an alloy which will contain the silicon in a form that is extractable by alkaline liquors.
- the alloy is reduced to a finely divided form, the silicon is extracted by means of alkaline liquors, and the residual skeleton of uranium metal powder is separated from the solution, washed, and dried.
- Uranium oxides are the starting material. I prefer to use U but other oxidation levels may be considered as well, provided they are readily available.
- the paste is prepared, for instance, as follows: Of the weight of the U 0 powder, approximately 2% potato starch flour, such as Knorr potato starch flour, are required. Thus, 6 parts by weight of potato starch flour are needed for 300 parts by weight of U 0 For each parts by weight of U 0 50 parts of cold water are needed. The calculated amount of potato flour is gradually stirred into the water which is then heated to boiling. A jelly is formed into which the U 0 powder is mixed. This procedure aims at having each U 0 particle well enveloped by the jelly. I have found that this is necessary if the subsequent reduction is to be performed successfully and without excessive formation of dross.
- (a) Drying The Si and U-bearing jelly obtained by operation (4) is dried at a temperature not exceeding 100 C.
- the gelatinous mass may be spread in form of a cake, for instance, on a sheet of metal, the bottom of which has previously been sprayed with machine oil to facilitate the release of the dried material.
- the metal sheet may be filled to two thirds of the height of its raised edge.
- Heating and reduction of the compressed pieces This may be done, for instance, as follows:
- uranium silicides are converted into an alloy which will contain the silicon in a form that can be leached by alkali. This is best done in a high-vacuum furnace in the absence of reactive compounds, for instance, in a protective atmosphere of gases of the helium group, such as helium, argon, neon. If no such gas is available, the material may, in an emergency, be treated under a cover of borax.
- the temperature of treatment may be raised just below the melting point of the alloy, which temperature may be 3 somewhere between 1,100 and .1,400 C., preferably between 1,200 and 1,300.
- the time of treatment is, for instance, three hours.
- the alloy of uranium and silicon thus'obtained is practicallyfree ofsilicides and con- "tains' the silicon in extractableform.
- the alloy is reduced topowder sothat'no.foreign.meta1s,fsuch as iron, are introduced (rolling mill with wheels .ofhard manganese steel or roller mill).
- the fineness of the powder should correspond, for instance, tothe German standard DIN 80 (screen with 6400 openings per square centimeter, 0.075 mm. diameterofthe opening).
- the uranium is extremely sensitive to NaOH (cobalt behaves similarly to uranium in this respect).
- NaOH such as 500 g./l. NaOH
- the extraction istherefore performed with diluted liquors containing, for instance, 40 to 70, preferably50 to 60 g./l. NaOH.
- the temperatures used are only slightly above room' temperature, that is, between '30, and 40 C., preferably 35-3 6 C. After this treatment, I prefer to run a controlanalysis to ascertain that 2.11 Si was dissolved. Otherwise, leaching must be continued under the conditions mentioned hereinbefore until practically all Si is dissolved.
- the uranium metal powder which remains undissolved in the characteristic skeleton form is thoroughly Washed in the usual way and then dried. 1
Landscapes
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Silicon Compounds (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH2905551X | 1954-12-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2905551A true US2905551A (en) | 1959-09-22 |
Family
ID=4572684
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US554909A Expired - Lifetime US2905551A (en) | 1954-12-24 | 1955-12-22 | Manufacturing of metallic uranium |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US2905551A (de) |
| CH (1) | CH333263A (de) |
| DE (1) | DE1013432B (de) |
| FR (1) | FR1143269A (de) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US854018A (en) * | 1905-09-23 | 1907-05-21 | Electro Metallurg Co | Process of reducing metallic oxids. |
| US866421A (en) * | 1907-01-31 | 1907-09-17 | Electro Metallurg Co | Process of effecting chemical reductions and producing metals or alloys. |
| US874977A (en) * | 1899-05-22 | 1907-12-31 | Charles Ludwig Rudolf Ernest Menges | Incandescent electric lamp. |
| US929578A (en) * | 1907-08-24 | 1909-07-27 | Gen Electric | Treating metal filaments. |
| US982135A (en) * | 1908-12-22 | 1911-01-17 | Gen Electric | Method of producing ferroboron. |
| US1019394A (en) * | 1910-07-20 | 1912-03-05 | Gen Electric | Reduction of chemical compounds. |
-
1954
- 1954-12-24 CH CH333263D patent/CH333263A/de unknown
-
1955
- 1955-12-16 FR FR1143269D patent/FR1143269A/fr not_active Expired
- 1955-12-22 US US554909A patent/US2905551A/en not_active Expired - Lifetime
- 1955-12-23 DE DEL23731A patent/DE1013432B/de active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US874977A (en) * | 1899-05-22 | 1907-12-31 | Charles Ludwig Rudolf Ernest Menges | Incandescent electric lamp. |
| US854018A (en) * | 1905-09-23 | 1907-05-21 | Electro Metallurg Co | Process of reducing metallic oxids. |
| US866421A (en) * | 1907-01-31 | 1907-09-17 | Electro Metallurg Co | Process of effecting chemical reductions and producing metals or alloys. |
| US929578A (en) * | 1907-08-24 | 1909-07-27 | Gen Electric | Treating metal filaments. |
| US982135A (en) * | 1908-12-22 | 1911-01-17 | Gen Electric | Method of producing ferroboron. |
| US1019394A (en) * | 1910-07-20 | 1912-03-05 | Gen Electric | Reduction of chemical compounds. |
Also Published As
| Publication number | Publication date |
|---|---|
| FR1143269A (fr) | 1957-09-27 |
| DE1013432B (de) | 1957-08-08 |
| CH333263A (de) | 1958-10-15 |
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