US1255144A - Process of obtaining tungstates. - Google Patents
Process of obtaining tungstates. Download PDFInfo
- Publication number
- US1255144A US1255144A US10635816A US10635816A US1255144A US 1255144 A US1255144 A US 1255144A US 10635816 A US10635816 A US 10635816A US 10635816 A US10635816 A US 10635816A US 1255144 A US1255144 A US 1255144A
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- US
- United States
- Prior art keywords
- sodium
- chlorid
- ore
- alkali
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G41/00—Compounds of tungsten
-
- 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
- C22B34/30—Obtaining chromium, molybdenum or tungsten
- C22B34/36—Obtaining tungsten
Definitions
- Our invention relates particularly to the treatment of ores containing heavy acid formingelements but particularly tungsten,
- the object of our invention is to obtain tungstic acid or a salt thereof, or a similar compound of any of the other heavy acidforming elements, by the treatment of various ores containing the same in such a manner as to separate out in a very complete manner the impurities contained in the ores and so as to obtain a compound of such element, as for example, a salt of tungstic acid, in a very pure form.
- a further object is to carry out this process by. the aid of fusion in such a manner that the impurities contained in the ore will become separated from the compound of' the heavy acid-forming element by sharp lines of demarcation in the fused bath and in: the resulting solid obtained by the cooling of the fused materials.
- a tungsten ore as for example, wolframite, hiibnerite, ferberite, scheelite, tungstite, etc., is crushed, sampled, and ground while dryin any suitablemanher, by any one of the well-known methods,
- the degree of fineness may vary to some extent with the nature of the ore, as for example, the facilitywith which it subjects itself to the succeeding treatments in the process.
- ground ore is then roasted in any suitable furnace so as to drive off the sulfur and arsenic contained in the ore as far as this is possible.
- the roasted ore is then mixed with sodium chlorid, sodium carbonate, and if found desirable, some silica.
- An amount of sodium chlorid is added, preferably from two-fifths to the same in-weight as the weight of theore.
- An amount of the sodium such ores the silica is omitted. If desired,
- sodiumnitrate or sodium chlorate may be added to the mixture which provide oxidizing agents in the bath'when fused.
- sodium chlorid we -may use sodium fluorid or calcium chlorid or fluorid.
- the charge is then fused in a suitable furnace. After thebath of fused materials has been allowed to cool, it will be found that the solid materialsiwill have become separated into a water soluble portion and a water insoluble portion, the tungstic acid being contained in the form of sodium tungstate in the water soluble portion.
- the sodium chlorid furthermore, acts to/dis,
- the sodium chlorid also acts as a solvent and diluent for the sodium carbonate It also plays a p in almost entirely preventing the formation of soluble silicates, phosphates, etc.
- the sodium chlorid also produces a crystalline structure with marked cleavage to the water soluble portion of the melt when solidified so that it is very friable and very easily crushed.
- the portion of the melt containing the sodium tungstate carries comparatively little unsodium chlorid and sodium carbonate permits the mass to be more readily melted than when the sodium chlorid is omitted, and the melted mass has a low viscosity so that the reacting fluid comes into contact with the particles of ore very readily.
- the extreme fluidity of the sodium carbonate and sodium chlorid when fused together renders it possible also to use less of the sodium carbonate than when the sodium chlorid is omitted. For the same reason it is possible to treat a coarser material in a shorter time than if the sodium chlorid were omitted.
- the sodium carbonate is provided for combining with the tungstic acid so as to produce sodium tungstate, and.
- an ore of another heavy acid-forming element may be similarly treated, as for example, an ore of chromium, molybdenum, vanadium or uranium, as for example, chromite, molybdenite or carnotite.
- fusing herein, and in the claims, we mean maintaining in a state of fusion and not necessarily passing from the solid to the liquid state.
- fusing in the claims we mean fusing one or more of the ingredients separately and mixing them together while fused or heating all of the ingredients together until fused.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Inorganic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Description
carried out in many difi'erent Ways, for the JOHN EKELEEY AND WILLIAM B. STODDALRID, OF BOULDER, COLORADO.
lhfiddnldd. I No Drawing.
To all whom it may concern:
Be it known that we, JOHN B. EKELEY and WILLIAM B. STonoARo, of Boulder, in the county of Boulder, and in the State of Colorado, have invented a certain new and useful Improvement in Processes of Obtaining Tungstates, and do hereby declare that the following is a full, clear, and exact description thereof.
Our invention relates particularly to the treatment of ores containing heavy acid formingelements but particularly tungsten,
so as to separate the impurities from the same and obtain the tungsten in the form of a salt of tungstic acid. It relates however also in a similar way tothe treatment of ores containing chromium, molybdenum, vanadium, or uranium, which are also heavy acid-forming elements.
The object of our invention is to obtain tungstic acid or a salt thereof, or a similar compound of any of the other heavy acidforming elements, by the treatment of various ores containing the same in such a manner as to separate out in a very complete manner the impurities contained in the ores and so as to obtain a compound of such element, as for example, a salt of tungstic acid, in a very pure form. A further object is to carry out this process by. the aid of fusion in such a manner that the impurities contained in the ore will become separated from the compound of' the heavy acid-forming element by sharp lines of demarcation in the fused bath and in: the resulting solid obtained by the cooling of the fused materials. Further objects of our invention will appear from the detailed description thereof appearing hereinafter. ile our invention is capable of being purpose of illustration we shall describe only one example of the several ways in which our invention may be followed.
As one example of the way in which our invention may be carried out we may proceed as follows: A tungsten ore, as for example, wolframite, hiibnerite, ferberite, scheelite, tungstite, etc., is crushed, sampled, and ground while dryin any suitablemanher, by any one of the well-known methods,
' to a suitable degree of fineness. The degree of fineness may vary to some extent with the nature of the ore, as for example, the facilitywith which it subjects itself to the succeeding treatments in the process The PROCESS OF OBTAINING- TUNGS'IATES.
- Specification of Letters Patent.
Patented net. for,
Application filed June as, 1916. Serial naioaeae.
ground ore is then roasted in any suitable furnace so as to drive off the sulfur and arsenic contained in the ore as far as this is possible. The roasted ore is then mixed with sodium chlorid, sodium carbonate, and if found desirable, some silica. An amount of sodium chlorid is added, preferably from two-fifths to the same in-weight as the weight of theore. An amount of the sodium such ores the silica is omitted. If desired,
sodiumnitrate or sodium chlorate may be added to the mixture which provide oxidizing agents in the bath'when fused. Instead of sodium chlorid, we -may use sodium fluorid or calcium chlorid or fluorid. The charge is then fused in a suitable furnace. After thebath of fused materials has been allowed to cool, it will be found that the solid materialsiwill have become separated into a water soluble portion and a water insoluble portion, the tungstic acid being contained in the form of sodium tungstate in the water soluble portion. The
solid mass, is crushed and then extracted with water and filtered. The filtrate is a clear solution of sodium tungstate which is pre-= cipitated as calcium tungstate by the addition of calcium chlorid in a sufficient quantity to replace all of the sodium by calcium 'in the sodium tungstate contained in the solution. v y
The sodium chloridperforms the function of producing sharp lines of demarcation between the two portions contained in the .fused bath and :in the resulting solid when cooled, the said two portions comprising a water soluble portion containing sodium tungstate, sodium carbonate and sodium chlorid, and a water insoluble portion comprising silicates and other materials derived from the gangue of themes treated. vThe sodium chlorid, furthermore, acts to/dis,
integrate and dissolve the tungsten ore with remarkable rapidity. The sodium chlorid also acts as a solvent and diluent for the sodium carbonate It also plays a p in almost entirely preventing the formation of soluble silicates, phosphates, etc. The sodium chlorid also produces a crystalline structure with marked cleavage to the water soluble portion of the melt when solidified so that it is very friable and very easily crushed. When sodium chlorid is used, the portion of the melt containing the sodium tungstate, carries comparatively little unsodium chlorid and sodium carbonate permits the mass to be more readily melted than when the sodium chlorid is omitted, and the melted mass has a low viscosity so that the reacting fluid comes into contact with the particles of ore very readily. The extreme fluidity of the sodium carbonate and sodium chlorid when fused together renders it possible also to use less of the sodium carbonate than when the sodium chlorid is omitted. For the same reason it is possible to treat a coarser material in a shorter time than if the sodium chlorid were omitted. The sodium carbonate is provided for combining with the tungstic acid so as to produce sodium tungstate, and. in the presence of the sodium chlorid the sodium carbonate also exerts a selective action on the tungstic acid in the ore by causing the sodium oxid contained in the same to combine with the tungstic acid in preference to the silica or phosphorus pentoxid, or other acid ingredients of the ore. Instead of treating a tungsten ore as above, an ore of another heavy acid-forming element may be similarly treated, as for example, an ore of chromium, molybdenum, vanadium or uranium, as for example, chromite, molybdenite or carnotite.
By the term fusing herein, and in the claims, we mean maintaining in a state of fusion and not necessarily passing from the solid to the liquid state. In other words, by the term fusing in the claims, we mean fusing one or more of the ingredients separately and mixing them together while fused or heating all of the ingredients together until fused.
While we have described our invention above in detail,-we wish it to be understood that many changes may be made therein without departing from the spirit of our invention.
We claim:
1. The process which comprises fusing a sodium carbonate when fused.
3. The process which comprises fusing a tungsten ore in a bath containing a halid of an alkali-forming metal, and a basic compound of an alkali-forming metal.
4. The process which comprises fusing a tungsten ore in a bath containing chlorid of sodium, and a basic compound of an alkali-forming metal.
5. The process which comprises fusing a tungsten ore in a bath'containing a halid of an alkali-forming metal and'sodium carbonate.
6. The process which comprises fusing a tungsten ore in a bath containing chlorid of sodium and sodium carbonate.
7. The process which comprises fusing a tungsten ore in a bath containing a halid of an alkali forming metal and an alkali and silica.
8. The process which comprises fusing a tungsten ore in a bath containing chlorid of sodium, an alkali and silica.
9. The process which comprises fusing a tungsten ore in a bath containing a halid of an alkali forming metal, sodium carbonate and silica.
10. The process which com-prises fusing a tungsten ore in a bath containing chlorid of sodium, sodium carbonate and silica.
11. The process which comprises fusing a tungsten ore in a bath'containing a halid of an alkali-forming metal, an alkali and an oxidizing salt.
12. The process which comprises fusing a tungsten ore in a bath containing a halid of an alkali-forming metal, an alkali and sodium nitrate.
13. The process which comprises grinding and roasting a tungsten ore, fusing the tungsten ore in a bath containing a halid of an alkali-forming metal, an alkali and an oxidizing salt.
14. The process which comprises grinding and roasting a tungsten ore, fusing the tungsten ore in a bath containing a halid of an alkali-forming metal, an alkali and sodium nitrate.
In testimony that we claim the foregoing we have hereunto set our hands.
JOHN B. EKELEY. WILLIAM B. STODDARD.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10635816A US1255144A (en) | 1916-06-28 | 1916-06-28 | Process of obtaining tungstates. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10635816A US1255144A (en) | 1916-06-28 | 1916-06-28 | Process of obtaining tungstates. |
Publications (1)
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US1255144A true US1255144A (en) | 1918-02-05 |
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US10635816A Expired - Lifetime US1255144A (en) | 1916-06-28 | 1916-06-28 | Process of obtaining tungstates. |
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2592421A (en) * | 1945-10-10 | 1952-04-08 | Smidth & Co As F L | Method of agglomerating finely divided materials |
US3259455A (en) * | 1962-05-09 | 1966-07-05 | Monsanto Co | Process for recovery of v-values from ferrophosphorus |
US3300276A (en) * | 1963-04-26 | 1967-01-24 | Degussa | Process for solubilizing vanadium values |
US3464783A (en) * | 1963-12-20 | 1969-09-02 | Egyesuelt Izzolampa | Process for working up ores which contain tungsten |
US3963824A (en) * | 1972-06-14 | 1976-06-15 | Produits Chimiques Ugine Kuhlmann | Process for extracting chromium from chromium ores |
US4080421A (en) * | 1976-01-29 | 1978-03-21 | Du Pont Of Canada Ltd. | Process for preparing ammonium tungstates |
US4083922A (en) * | 1976-01-29 | 1978-04-11 | Du Pont Of Canada Limited | Process for the manufacture of ammonium and alkali metal tungstates |
US4603043A (en) * | 1985-03-01 | 1986-07-29 | Gte Products Corporation | Controllable nitrate fusion |
WO1990008103A1 (en) * | 1989-01-23 | 1990-07-26 | Kennametal Inc. | Process for producing tungsten monocarbide |
US5096689A (en) * | 1989-01-23 | 1992-03-17 | Kennametal Inc. | Process for producing tungsten monocarbide |
JPH05501770A (en) * | 1989-11-06 | 1993-04-02 | サーノフ コーポレイション | Dynamic object recognition method and its image processing system |
-
1916
- 1916-06-28 US US10635816A patent/US1255144A/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2592421A (en) * | 1945-10-10 | 1952-04-08 | Smidth & Co As F L | Method of agglomerating finely divided materials |
US3259455A (en) * | 1962-05-09 | 1966-07-05 | Monsanto Co | Process for recovery of v-values from ferrophosphorus |
US3300276A (en) * | 1963-04-26 | 1967-01-24 | Degussa | Process for solubilizing vanadium values |
US3464783A (en) * | 1963-12-20 | 1969-09-02 | Egyesuelt Izzolampa | Process for working up ores which contain tungsten |
US3963824A (en) * | 1972-06-14 | 1976-06-15 | Produits Chimiques Ugine Kuhlmann | Process for extracting chromium from chromium ores |
US4080421A (en) * | 1976-01-29 | 1978-03-21 | Du Pont Of Canada Ltd. | Process for preparing ammonium tungstates |
US4083922A (en) * | 1976-01-29 | 1978-04-11 | Du Pont Of Canada Limited | Process for the manufacture of ammonium and alkali metal tungstates |
US4603043A (en) * | 1985-03-01 | 1986-07-29 | Gte Products Corporation | Controllable nitrate fusion |
WO1990008103A1 (en) * | 1989-01-23 | 1990-07-26 | Kennametal Inc. | Process for producing tungsten monocarbide |
US5096689A (en) * | 1989-01-23 | 1992-03-17 | Kennametal Inc. | Process for producing tungsten monocarbide |
JPH05501770A (en) * | 1989-11-06 | 1993-04-02 | サーノフ コーポレイション | Dynamic object recognition method and its image processing system |
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