US1945074A - Recovery of selenium - Google Patents
Recovery of selenium Download PDFInfo
- Publication number
- US1945074A US1945074A US494923A US49492330A US1945074A US 1945074 A US1945074 A US 1945074A US 494923 A US494923 A US 494923A US 49492330 A US49492330 A US 49492330A US 1945074 A US1945074 A US 1945074A
- Authority
- US
- United States
- Prior art keywords
- copper
- selenium
- slag
- treating
- ore
- 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
- 239000011669 selenium Substances 0.000 title description 23
- 229910052711 selenium Inorganic materials 0.000 title description 23
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 title description 21
- 238000011084 recovery Methods 0.000 title description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 28
- 239000002893 slag Substances 0.000 description 28
- 239000000047 product Substances 0.000 description 21
- 238000000034 method Methods 0.000 description 16
- 230000001603 reducing effect Effects 0.000 description 12
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 11
- 239000005864 Sulphur Substances 0.000 description 11
- 229910052802 copper Inorganic materials 0.000 description 11
- 239000010949 copper Substances 0.000 description 11
- BWFPGXWASODCHM-UHFFFAOYSA-N copper monosulfide Chemical compound [Cu]=S BWFPGXWASODCHM-UHFFFAOYSA-N 0.000 description 11
- 238000003723 Smelting Methods 0.000 description 9
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 8
- 150000001339 alkali metal compounds Chemical class 0.000 description 7
- 229910001361 White metal Inorganic materials 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 239000010969 white metal Substances 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 3
- 150000001340 alkali metals Chemical class 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 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 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 125000003748 selenium group Chemical group *[Se]* 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- -1 sodium and potassium Chemical class 0.000 description 2
- 229910000897 Babbitt (metal) Inorganic materials 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 241001625808 Trona Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 229910001948 sodium oxide Inorganic materials 0.000 description 1
- VPQBLCVGUWPDHV-UHFFFAOYSA-N sodium selenide Chemical compound [Na+].[Na+].[Se-2] VPQBLCVGUWPDHV-UHFFFAOYSA-N 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 235000010269 sulphur dioxide Nutrition 0.000 description 1
- 239000004291 sulphur dioxide Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/006—Pyrometallurgy working up of molten copper, e.g. refining
Definitions
- This invention relates to metallurgy and has for an object the provision of an improved process for treating copper ores. More particularly, the invention contemplates the provision of an improved process for obtaining a copper product suitable for purification by electrolysis. The invention further contemplates the provision of a process for recovering selenium from metal products.
- Copper ores frequently contain, in addition to iron and other gangue materials, impurities such as arsenic, antimony, selenium and telluriurn, some of which are eliminated during smelting operations and others of which are retained by 15 the blister copper and eliminated during the electrolytic operations.
- impurities may be present in commercial amounts and in sufficiently large quantities to reduce the efficiency of the electrolytic operations.
- the independent producers may send their blister copper to custom refineries for treatment.
- the producers may be penalized by the refiners, and, in some instances, notably in the case of selenium, even though the blister copper contains commercial amounts of the so-called impurities, no credit is given the producers.
- the present invention is based on our discovery that a relatively pure copper product may be obtained by subjecting blister copper or the product of a converting operation between the stages of white metal and blister copper, in the form of a molten bath, to the action of a slag containing one or more alkali metal compounds.
- a slag containing one or more alkali metal compounds we have found that such slags are particularly effective for recovering selenium.
- the treatment for the recovery of selenium is most effective when conducted in a reducing environment.
- a highly basic slag containing an amount of alkali metal oxide in excess of that which is satisfied by the acid forming constituents may be employed.
- Slags for use in the process of the invention may be formed in any desired manner.
- Alkali metal oxides, or other suitable compounds of alkali metals like sodium and potassium, may be applied to the surface of a molten copper bath, or, molten copper may be treated with an alkali metal such, for example, as metallic sodium in the presence of sufficient non-metallic oxides to form a slag with the resulting sodium oxide, sodium sulphide, and sodium selenide.
- the ore In treating a selenium-bearing copper sulphide ore for the recovery of selenium, the ore is first smelted in a blast or reverberatory furnace tr. Q produce a matte suitable for converting.
- the matte is placed in a converter and treated in the usual manner until white metal has been produced.
- the white metal is blown until a product containing about two percent sulphur is obtained.
- This product is then transferred from the converter to a suitable furnace such, for example, as a refining furnace and covered with a layer of slag containing an alkali metal compound, preferably, a soda slag.
- a suitable furnace such, for example, as a refining furnace and covered with a layer of slag containing an alkali metal compound, preferably, a soda slag.
- the slag covered bath is agitated and subjected to the action of a reducing agent.
- the reducing action and agitation may be accomplished by injecting oil, reducing gas, powdered coal or coke through tuyeres below the surface of the bath or by poling. Agitation may be continued until the sulphur and selenium are substantially completely eliminated from the copper of the bath.
- the purified copper may be cast into molds.
- the selenium will be found in the slag, probably in the form of an alkali metal selenide which may be placed in solution by leaching with water.
- the selenium may be recovered from the solution in 1 any suitable manner, as, for example, by passing air or sulphur dioxide through the solution to effect precipitation.
- the slag may be treated for the recovery of selenium after treating a single batch of copper or an enriched product may be obtained by using the same slag for treating several batches.
- the method of recovering selenium from copper sulphide ore which comprises smelting the ore to produce matte, subjecting the matte to a converting operation until a product containing a small percentage of sulphur is obtained, subjecting the resulting product in the from of a molten bath to the action of a soda slag under reducing conditions, and treating the slag to recover selenium.
- the method of recovering selenium from copper sulphide ore which comprises treating the ore to form a molten bath of blister copper, subjecting the blister copper to the action of a slag containing one or more alkali metal compounds under reducing conditions, and treating the slag to recover selenium.
- the method of recovering selenium from copper sulphide ore which comprises treating the ore to form a molten bath of blister copper, subjecting the blister copper to the action of a soda slag under reducing conditions, and treating the slag to recover selenium.
- the method of recovering selenium from copper sulphide ore which comprises treating the ore to form a molten bath of blister copper and subjecting the molten blister copper to the action of an alkali metal in the presence of one or more slag forming compounds.
- the method of treating selenium-bearing metal to remove the selenium therefrom comprises subjecting the metal in the form of a molten bath to the action of a slag containing OLIVER C. RALSTON. LEONARD KLEIN.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented Jan. 30, 1934 UNITED STATES PATENT QFFICE Aria, assignors to United Verde Copper Company, a corporation of Delaware No Drawing.
Application November 11, 1930 Serial No. 494,923
12 Claims.
This invention relates to metallurgy and has for an object the provision of an improved process for treating copper ores. More particularly, the invention contemplates the provision of an improved process for obtaining a copper product suitable for purification by electrolysis. The invention further contemplates the provision of a process for recovering selenium from metal products.
Copper ores frequently contain, in addition to iron and other gangue materials, impurities such as arsenic, antimony, selenium and telluriurn, some of which are eliminated during smelting operations and others of which are retained by 15 the blister copper and eliminated during the electrolytic operations. The impurities may be present in commercial amounts and in sufficiently large quantities to reduce the efficiency of the electrolytic operations.
It is customary for the independent producers to send their blister copper to custom refineries for treatment. When the blister copper contains harmful impurities, the producers may be penalized by the refiners, and, in some instances, notably in the case of selenium, even though the blister copper contains commercial amounts of the so-called impurities, no credit is given the producers.
It is desirable to so conduct metallurgical operations for the treatment of copper ores as to avoid the incorporation of impurities in the blister copper in order to improve the eiliciency of the electrolytic operations and/or to recover a valuable commercial product.
The present invention is based on our discovery that a relatively pure copper product may be obtained by subjecting blister copper or the product of a converting operation between the stages of white metal and blister copper, in the form of a molten bath, to the action of a slag containing one or more alkali metal compounds. We have found that such slags are particularly effective for recovering selenium. The treatment for the recovery of selenium is most effective when conducted in a reducing environment.
In carrying out the process of the invention, we prefer to employ a highly basic slag containing an amount of alkali metal oxide in excess of that which is satisfied by the acid forming constituents. Slags for use in the process of the invention may be formed in any desired manner. Alkali metal oxides, or other suitable compounds of alkali metals like sodium and potassium, may be applied to the surface of a molten copper bath, or, molten copper may be treated with an alkali metal such, for example, as metallic sodium in the presence of sufficient non-metallic oxides to form a slag with the resulting sodium oxide, sodium sulphide, and sodium selenide.
As a result of our discovery, we propose to 0 modify the usual copper smelting practice to include a step involving the treatment of blister copper, or the product of the converting operation immediately before it reaches the blister copper stage, in the form of a molten bath, with a slag containing one or more alkali metal compounds. The converting operation is continued until impurities such as iron and other gangue materials have been eliminated and white metal has been produced. Blowing of the white metal 7 may be continued until the blister copper stage has been reached, but it is preferably discontinued when the major portion of the sulphur has been eliminated. We have found that a white metal or blister copper product containing about two percent of sulphur may be treated effectively.
In treating a selenium-bearing copper sulphide ore for the recovery of selenium, the ore is first smelted in a blast or reverberatory furnace tr. Q produce a matte suitable for converting. The matte is placed in a converter and treated in the usual manner until white metal has been produced. The white metal is blown until a product containing about two percent sulphur is obtained. This product is then transferred from the converter to a suitable furnace such, for example, as a refining furnace and covered with a layer of slag containing an alkali metal compound, preferably, a soda slag. We have used, successfully, slags formed from trona, an impure sodium carbonate containing about five percent lime.
The slag covered bath is agitated and subjected to the action of a reducing agent. The reducing action and agitation may be accomplished by injecting oil, reducing gas, powdered coal or coke through tuyeres below the surface of the bath or by poling. Agitation may be continued until the sulphur and selenium are substantially completely eliminated from the copper of the bath. The purified copper may be cast into molds. The selenium will be found in the slag, probably in the form of an alkali metal selenide which may be placed in solution by leaching with water. The selenium may be recovered from the solution in 1 any suitable manner, as, for example, by passing air or sulphur dioxide through the solution to effect precipitation.
The slag may be treated for the recovery of selenium after treating a single batch of copper or an enriched product may be obtained by using the same slag for treating several batches.
We claim:--
1. The method of treating copper sulphide ore which comprises smelting the ore to produce matte, treating the matte to eliminate sulphur, and subjecting the resulting product in the form of a molten bath to the action of a slag containing one or more alkali metal compounds under reducing conditions.
2. The method of treating copper sulphide ore which comprises smelting the ore to produce matte, treating the matte to eliminate sulphur, and subjecting the resulting product in the form of a molten bath to the action of a slag containing one or more alkali metal oxides under reducing conditions.
3. The method of treating copper sulphide ore which comprises smelting the ore to produce matte, treating the matte to obtain a product containing about two-percent sulphur, and subjecting the resulting product in the form of a molten bath to the action of a slag containing one or more alkali metal compounds under reducing conditions.
4. The method of treating copper sulphide ore which comprises smelting the ore to produce matte, treating the matte to obtain a product containing about two-percent sulphur, and subjecting the resulting product in the form of a molten bath to the action of a soda slag under reducing conditions.
5. The method of treating copper sulphide ore which comprises smelting the ore to produce matte, subjecting the matte to a converting operation until a molten product containing about two-percent sulphur is obtained, and subjecting the resulting product to the action of a soda slag under reducing conditions.
6. The method of recovering selenium from copper sulphide ore which comprises smelting the ore to produce matte, subjecting the matte to a converting operation until a product containing a small percentage of sulphur is obtained, subjecting the resulting product in the form of a molten bath to the action of a slag containing one or more alkali metal compounds under reducing conditions, and treating the slag to recover selenium.
'7. The method of recovering selenium from copper sulphide ore which comprises smelting the ore to produce matte, subjecting the matte to a converting operation until a product containing a small percentage of sulphur is obtained, subjecting the resulting product in the from of a molten bath to the action of a soda slag under reducing conditions, and treating the slag to recover selenium.
8. The method of recovering selenium from copper sulphide ore which comprises treating the ore to form a molten bath of blister copper, subjecting the blister copper to the action of a slag containing one or more alkali metal compounds under reducing conditions, and treating the slag to recover selenium.
9. The method of recovering selenium from copper sulphide ore which comprises treating the ore to form a molten bath of blister copper, subjecting the blister copper to the action of a soda slag under reducing conditions, and treating the slag to recover selenium.
10. The method of recovering selenium from copper sulphide ore which comprises treating the ore to form a molten bath of blister copper and subjecting the molten blister copper to the action of an alkali metal in the presence of one or more slag forming compounds.
11. The method of treating selenium-bearing metal to remove the selenium therefrom which comprises subjecting the metal in the form of a molten bath to the action of a slag containing OLIVER C. RALSTON. LEONARD KLEIN.
subjecting the metal in the form of a ii
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US494923A US1945074A (en) | 1930-11-11 | 1930-11-11 | Recovery of selenium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US494923A US1945074A (en) | 1930-11-11 | 1930-11-11 | Recovery of selenium |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1945074A true US1945074A (en) | 1934-01-30 |
Family
ID=23966516
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US494923A Expired - Lifetime US1945074A (en) | 1930-11-11 | 1930-11-11 | Recovery of selenium |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1945074A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2816008A (en) * | 1955-12-06 | 1957-12-10 | American Smelting Refining | Recovery of selenium from scrap selenium rectifiers |
| US2834652A (en) * | 1956-10-01 | 1958-05-13 | American Smelting Refining | Recovery of selenate values contained in sulfuric acid solutions |
| US2835558A (en) * | 1955-08-09 | 1958-05-20 | Diamond Alkali Co | Recovery of selenium |
| US3772001A (en) * | 1971-12-14 | 1973-11-13 | American Smelting Refining | Process for de-selenizing copper |
| US4055415A (en) * | 1975-04-16 | 1977-10-25 | Csepeli Femmu | Process for the removal of alloying impurities in a slag-covered copper refining bath |
-
1930
- 1930-11-11 US US494923A patent/US1945074A/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2835558A (en) * | 1955-08-09 | 1958-05-20 | Diamond Alkali Co | Recovery of selenium |
| US2816008A (en) * | 1955-12-06 | 1957-12-10 | American Smelting Refining | Recovery of selenium from scrap selenium rectifiers |
| US2834652A (en) * | 1956-10-01 | 1958-05-13 | American Smelting Refining | Recovery of selenate values contained in sulfuric acid solutions |
| US3772001A (en) * | 1971-12-14 | 1973-11-13 | American Smelting Refining | Process for de-selenizing copper |
| US4055415A (en) * | 1975-04-16 | 1977-10-25 | Csepeli Femmu | Process for the removal of alloying impurities in a slag-covered copper refining bath |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1945074A (en) | Recovery of selenium | |
| US4135912A (en) | Electric smelting of lead sulphate residues | |
| US1809871A (en) | Production of bismuth | |
| US2264337A (en) | Metallurgy of zinc fumes and other powdery metalliferous material containing zinc and other metals | |
| US2365177A (en) | Process for refining lead or lead alloys | |
| US1950387A (en) | Slag formation and reduction in lead softening | |
| US2042291A (en) | Process for refining copper alloys | |
| GB123272A (en) | Process of Treating Lead Bullion. | |
| US2343760A (en) | Smelting of drosses, mattes, and the like | |
| US1642358A (en) | Method of treating lead dross | |
| US1593509A (en) | Process for the recovery of metal and other values in ores | |
| US1989734A (en) | Production of bismuth | |
| US1827821A (en) | Reduction of metal compounds | |
| US1518626A (en) | Treatment of copper-lead matte | |
| US1868414A (en) | Method of recovering cobalt | |
| US722809A (en) | Method of treating ores. | |
| US1806310A (en) | Recovery of metals | |
| US308031A (en) | John j | |
| US1816743A (en) | Recovery of metals from ores | |
| US1461957A (en) | Process of recovering tin from impure ores | |
| US1438643A (en) | Recovery of zinc | |
| US1097897A (en) | Method of treating antimony and arsenic ores. | |
| US1827820A (en) | Treatment of metals and/or their compounds | |
| US1265547A (en) | Extraction of lead from its ores or lead-containing materials. | |
| US575467A (en) | Francis ellershatjsen |