US679997A - Electrolytic process of obtaining metals from their fused compounds. - Google Patents
Electrolytic process of obtaining metals from their fused compounds. Download PDFInfo
- Publication number
- US679997A US679997A US69645498A US1898696454A US679997A US 679997 A US679997 A US 679997A US 69645498 A US69645498 A US 69645498A US 1898696454 A US1898696454 A US 1898696454A US 679997 A US679997 A US 679997A
- Authority
- US
- United States
- Prior art keywords
- sulfid
- bath
- fused
- electrolysis
- electrolytic process
- 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
- 229910052751 metal Inorganic materials 0.000 title description 19
- 239000002184 metal Substances 0.000 title description 18
- 150000001875 compounds Chemical class 0.000 title description 15
- 238000000034 method Methods 0.000 title description 14
- 150000002739 metals Chemical class 0.000 title description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 18
- 238000005868 electrolysis reaction Methods 0.000 description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 9
- 229910052717 sulfur Inorganic materials 0.000 description 9
- 239000011593 sulfur Substances 0.000 description 9
- 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 8
- 229910052708 sodium Inorganic materials 0.000 description 8
- 239000011734 sodium Substances 0.000 description 8
- 235000011121 sodium hydroxide Nutrition 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 3
- 230000004927 fusion Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/02—Electrolytic production, recovery or refining of metals by electrolysis of melts of alkali or alkaline earth metals
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
Definitions
- my invention consists in the employment in the electrolytic production of metal by fused-bath electrolysis of an electrolyte composed of a mixture of a sulfid and another more fusible compound of the metal desired, which is easily conyertible into a sulfid by nascent sulfur.
- I prepare an electrolytic bath composed of about equal parts of sodium sulfid and caustic soda. Although the meltingpoint of so dium sulfid is, as has been stated, high, the melting-point of this combination is not very much above that of caustic soda.
- the bath having been heated to fusion, I then pass an electric current bet-ween suitable anodes through the fused electrolyte. By reason of the presence of the sulfid a very much lower voltage may be used than would be required if caustic soda alone were used.
- the theoretical voltage of the decomposition of sodium sulfid is one and eight-tenths volts; but I have been able to elfect the decomposition of my electrolyte when the voltage absorbed in decomposition is considerably lower, going down as low as one and two-tenths volts, and sometimes even lower. I maintain the current at such a low voltage that the current decomposes the sulfid only, liberating the metallic element at the cathode, which is collected in the usual manner. Sulfur is liberated at the anode in. 3mm nascent, the cansticsodaimmediatelyconvertingitintosodium sultid.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Description
UNITED STATES PATENT OFFICE.
GEORGE I. SOHOLL, OF PHILADELPHIA, PENNSYLVANIA, ASSIGNOR TO CHARLES W. ROEPPER, OF SAME PLACE.
ELECTROLYTIC PROCESS OF OBTAINING METALS FROM THEIR FUSED COMPOUNDS.
SPECIFICATION formingpart of Letters Patent No. 679,997, dated August 6, 1901.
Application filed November 14,1898. 1
To all whom it may concern: I
Be it known that I, GEORGE P. SOHOLL, a subject of the Emperor of Germany, residing in Philadelphia, in the State of Pennsylvania, have invented certain new and useful Improvements in Electrolytic Processes for Obtaining Metals from Their Fused Compounds, whereof the following is a specification.
In the various processes which havehitherto been invented and used for the purpose of electrolytically deriving metals from their fused compounds the use of metallic sulfid as the compound to be decomposed electrolytically in its fused state has been avoided by reason of the exceedingly high fusing-point of sulfids as a class. Thus, for example, sodium sullid is fusible only at a temperature much above the point at which metallic sodium vaporizes. Its use, therefore, in the electrolytic production of metallic sodium is difficult.
I have discovered that by using an initial proportion of sulfid in combination with a more fusible compound of the same metal a fusible electrolytic bath may be prepared without unduly increasing the temperature requisite for fusion, and in this way Iam enabled to take advantage of the very low electromotive force required for the decomposition of a bath containing a sultid. Furthermore, by continuously renewing the non sulfur component of the bath I find that this-ad vantage may be maintained continuously,
little if any more of the comparatively expensive sulfid being needed.
In order to carryout this process, it is only necessary to choose for the non-sulfur component of the bath a comparatively fusible compound of the metal desired, which is easily convertible into 'asulfid by the sulfur generated at the anode by the electrolysis of the sulfid.
Briefly stated, therefore, my invention consists in the employment in the electrolytic production of metal by fused-bath electrolysis of an electrolyte composed of a mixture of a sulfid and another more fusible compound of the metal desired, which is easily conyertible into a sulfid by nascent sulfur.
I will describe my invention as I practice it in the production of metallic sodium, pre- Serial No. 696,454 (No specimens.)
mising that it is applicable under the conditions which have just been stated to the production of other metals and that the specific mention'of sodium is typical and not restrictive.
I prepare an electrolytic bath composed of about equal parts of sodium sulfid and caustic soda. Although the meltingpoint of so dium sulfid is, as has been stated, high, the melting-point of this combination is not very much above that of caustic soda. The bath having been heated to fusion, I then pass an electric current bet-ween suitable anodes through the fused electrolyte. By reason of the presence of the sulfid a very much lower voltage may be used than would be required if caustic soda alone were used. The theoretical voltage of the decomposition of sodium sulfid is one and eight-tenths volts; but I have been able to elfect the decomposition of my electrolyte when the voltage absorbed in decomposition is considerably lower, going down as low as one and two-tenths volts, and sometimes even lower. I maintain the current at such a low voltage that the current decomposes the sulfid only, liberating the metallic element at the cathode, which is collected in the usual manner. Sulfur is liberated at the anode in. 3mm nascent, the cansticsodaimmediatelyconvertingitintosodium sultid. By continuously supplying caustic soda as fast as the sodium is produced at the cathode the proportion of sodium sulfid is kept constant, the process proceeding continuously, as has been described. In this way it will be observed that the electrolysis is to all intents and purposes the electrolysis of a suliid salt only, and yet a small initial quantity of the comparatively expensive sulfid is all that need be introduced, and this is rendered readily fusible by admixture with the other compound.
I have not yet been able to ascertain with certainty the reactions which take place; but they appear to be complicated by the presence of polysulfids.
I may here point out certain advantages which the process thus described presents over processes for obtaining metallic sodium by the electrolysis of caustic soda. These are the economic advantage of low-voltage ourrent and the absence of that very considerable element of danger in the caustic-soda process which results from the generation of hydrogen at the cathode. Owing to the heat at which the process is carried on the hydrogen so generated frequently explodes. To avoid this danger in such processes, very small plants have to be used. In my process there being less hydrogen liberated and that under a lower temperature, a single plant may be safely enlarged, 'so as to have a very great productive capacity with consequent economy of operation.
i In obtaining metals other than sodium other compounds than the hydroxids may be used as the non-sulfur component of the bath; but the choice of this component is clearly indicated by two conditions. It must be a comparatively fusible compound of the desired metal, and it must be one which is convertible into a sullid by nascent sulfur.
subjecting the fused bath to electrolysis by the action of suitable electrodes, substantially asdescribe'd. I
2. The process of obtaining metals by the electrolysis of their fused compounds, which consists in fusing a bath composed of a mixture of sulfid of the desired metal'w-ith a more fusible compound of said metal which is convertible into sulfid by nascent sulfur; and subjecting the fused bath to electrolysis by the action of suitable electrodes under a current which will decompose the sulfid only, substantially as described.
'3. The process of obtaining metals by the electrolysis of their fused compounds, which consists in fusing a bath composed of a mixture of sulfid of the desired metal with a more fusible compound of said metal which is convertible into sulfid by nascent sulfur; subjecting the fused bath to electrolysis by the action of suitable electrodes under a current which will decompose the sulfid only; and continuously renewing the bath by addition of the other constituents in proportion as the metal ingredient is liberated at the
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US69645498A US679997A (en) | 1898-11-14 | 1898-11-14 | Electrolytic process of obtaining metals from their fused compounds. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US69645498A US679997A (en) | 1898-11-14 | 1898-11-14 | Electrolytic process of obtaining metals from their fused compounds. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US679997A true US679997A (en) | 1901-08-06 |
Family
ID=2748543
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US69645498A Expired - Lifetime US679997A (en) | 1898-11-14 | 1898-11-14 | Electrolytic process of obtaining metals from their fused compounds. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US679997A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2660514A (en) * | 1949-04-08 | 1953-11-24 | Frederick A Rohrman | Removal of nitrogen from mixtures of combustible gases |
| US3531386A (en) * | 1967-05-15 | 1970-09-29 | North American Rockwell | Electrochemical process for recovering sulfur values |
| US5009751A (en) * | 1988-01-12 | 1991-04-23 | Mitsubishi Nuclear Fuel Company, Ltd. | Process for separation of hafnium tetrachloride from zirconium tetrachloride |
-
1898
- 1898-11-14 US US69645498A patent/US679997A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2660514A (en) * | 1949-04-08 | 1953-11-24 | Frederick A Rohrman | Removal of nitrogen from mixtures of combustible gases |
| US3531386A (en) * | 1967-05-15 | 1970-09-29 | North American Rockwell | Electrochemical process for recovering sulfur values |
| US5009751A (en) * | 1988-01-12 | 1991-04-23 | Mitsubishi Nuclear Fuel Company, Ltd. | Process for separation of hafnium tetrachloride from zirconium tetrachloride |
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