US903732A - Copper-leaching process. - Google Patents
Copper-leaching process. Download PDFInfo
- Publication number
- US903732A US903732A US42730608A US1908427306A US903732A US 903732 A US903732 A US 903732A US 42730608 A US42730608 A US 42730608A US 1908427306 A US1908427306 A US 1908427306A US 903732 A US903732 A US 903732A
- Authority
- US
- United States
- Prior art keywords
- copper
- chlorid
- solution
- sulfur dioxid
- leaching 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
- 238000000034 method Methods 0.000 title description 13
- 238000002386 leaching Methods 0.000 title description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical class [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 11
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 10
- 239000010949 copper Substances 0.000 description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- SURLGNKAQXKNSP-DBLYXWCISA-N chlorin Chemical compound C\1=C/2\N/C(=C\C3=N/C(=C\C=4NC(/C=C\5/C=CC/1=N/5)=CC=4)/C=C3)/CC\2 SURLGNKAQXKNSP-DBLYXWCISA-N 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G49/00—Compounds of iron
- C01G49/10—Halides
Definitions
- the process relates to the leaching of oxidized copper ores with a dilute solution of sulfuric acid which contains chlorin in the form of a chlorid of some sort, (such as sodium chlorid, ferrous chlorid or calcium chlorid); in quantity suflicient to form the sub-chlorid with the copper which goes into the solution and it consists in the novel mode of procedure hereinafter described.
- chlorid such as sodium chlorid, ferrous chlorid or calcium chlorid
- the improved method of working which consists in absorbing the sulfur dioxid in the cold copper solution and then heating under pressure to completethereaction between the sulfur dioxid and the cupric chlorid.
- the method they pursued was to inject sulfur dioxid into the hot copper solution.
- the sulfur dioxid obtained in practice always contains some oxygen.
- an oxidation of the precipitated cuprous chlorid always accompanies the reduction of the cupric chlorid which makes it impossible to obtain a complete conversion of the cop er into cuprous chlorid.
- my method t is does not take place, since the oxygen comes in contact only with the cold solution and before the formation of cuprous chlorid has properly started.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
FREDERICK LAIST, CE BUTTE, MONTANA.
COPPER-REACHING PROCESS.
Specification of Letters Patent.-
Application filed April 16, 1908. Serial No. 427,306.
Patented Nov. 10, 19 08.
To all whom it may concern:
Be it known that I, FREDERICK LAIST, a citizen of the United States, residing at Butte, in the county of Silverbow and State of Montana, have invented a new and useful Improvement in Copper-Leaching Processes, of which the following is a specification.
The process relates to the leaching of oxidized copper ores with a dilute solution of sulfuric acid which contains chlorin in the form of a chlorid of some sort, (such as sodium chlorid, ferrous chlorid or calcium chlorid); in quantity suflicient to form the sub-chlorid with the copper which goes into the solution and it consists in the novel mode of procedure hereinafter described.
Having dissolved the copper from the ore, it is to be precipitated from the resultant solution as the sub-chlorid, or cuprous I chlorid, (Cu cl This is done preferably by running the cold solution down an absorbent tower up which sulfur dioxid gases,-
(generated by burning pyrites, sulfur, etc.,) are passing. The sulfur dioxid is absorbed by the cold solution, so that I obtain a solution containing 2% to 4% of sulfur dioxid. The percentage of sulfur dioxid gas absorbed must be at least one half of the per cent. of copper which the solution contains. This solution is now run into a boiler, lined with an acid proof metal, and containing steam coils for heating and a safety valve adjusted to go off at about 15 lbs. pressure.
Here it is brought to boiling and the'fol lowing reaction takes place.
or more simply stated I quantities of ore.
1 I am aware that the reactions of this process have been already described in patents later as the Hunt and Douglas process. My
invention is distinguished therefrom by the improved method of working, which consists in absorbing the sulfur dioxid in the cold copper solution and then heating under pressure to completethereaction between the sulfur dioxid and the cupric chlorid. The method they pursued was to inject sulfur dioxid into the hot copper solution. This method'is not nearly so economical of sulfur dioxid nor so convenient of manipulation as my method. Moreover the sulfur dioxid obtained in practice always contains some oxygen. Hence an oxidation of the precipitated cuprous chlorid always accompanies the reduction of the cupric chlorid which makes it impossible to obtain a complete conversion of the cop er into cuprous chlorid. In my method t is does not take place, since the oxygen comes in contact only with the cold solution and before the formation of cuprous chlorid has properly started.
Heating under pressure, very materially I aids the reduction, because it keeps the sulfur dioxid in the solutionuntil the reaction temperature, (which is near 100 C.) is reached. It is very difiicult to obtain a precipitation of more than 75% of the copper in the solution when heating in the open. Under pressure, 90% to 95% can be brought down. In fact the completeness of precipitation is limited only by the slight solubility of cuprous chlorid."
I claim The process of precipitating copper from a chloridiz'ed solution as the sub-chlorid, which consists in first dissolving inthe cold solution a quantity ofsulfur dioxid, and then heating this solution, under pressure, to complete the reduction of the cupr c chlorid to cuprous chlorid. Y
FREDERICK LAIST.
.Witnesses JAMES E. MURRAY, HOWARD K. WELCH. v
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US42730608A US903732A (en) | 1908-04-16 | 1908-04-16 | Copper-leaching process. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US42730608A US903732A (en) | 1908-04-16 | 1908-04-16 | Copper-leaching process. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US903732A true US903732A (en) | 1908-11-10 |
Family
ID=2972159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US42730608A Expired - Lifetime US903732A (en) | 1908-04-16 | 1908-04-16 | Copper-leaching process. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US903732A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3647368A (en) * | 1970-04-09 | 1972-03-07 | Morton Norwich Products Inc | Use of sodium chloride in providing aqueous solutions of copper salts from copper ore |
| US4715939A (en) * | 1986-04-22 | 1987-12-29 | Cominco Ltd. | Method for removal of monovalent ions from ZnSO4 electrolyte by electrodialysis |
-
1908
- 1908-04-16 US US42730608A patent/US903732A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3647368A (en) * | 1970-04-09 | 1972-03-07 | Morton Norwich Products Inc | Use of sodium chloride in providing aqueous solutions of copper salts from copper ore |
| US4715939A (en) * | 1986-04-22 | 1987-12-29 | Cominco Ltd. | Method for removal of monovalent ions from ZnSO4 electrolyte by electrodialysis |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| BRPI0611358A2 (en) | method for the recovery of precious metals and arsenic from a solution | |
| EP0047742B1 (en) | A process for recovering non-ferrous metal values from ores, concentrates, oxidic roasting products or slags | |
| US903732A (en) | Copper-leaching process. | |
| US3499754A (en) | Process for purifying pyrite cinders by removal of nonferrous metals | |
| US287737A (en) | Gael a | |
| US1937661A (en) | Dry chloridizing of ores | |
| US2653905A (en) | Process for total treatment of copper-containing iron pyrites | |
| US1943332A (en) | Method of chloridizing ores by means of ferric chloride | |
| US198776A (en) | Improvement in recovery of waste nitrous gases | |
| US1102715A (en) | Purification of mixtures containing nitrids. | |
| US401056A (en) | office | |
| US2067778A (en) | Method of treating complex lead bearing ore materials | |
| US2025068A (en) | Method of treating sulphide ores | |
| US203849A (en) | Improvement in treating ores of zinc | |
| US718554A (en) | Method of extracting zinc. | |
| US544319A (en) | And william p | |
| US1083910A (en) | Process of production of lead solutions from lead ore. | |
| US1300417A (en) | Process of preparing alumina. | |
| US1719534A (en) | Treatment of sulphur-bearing minerals | |
| US1508561A (en) | Treatment of sulphide ore with nitrates | |
| US1918178A (en) | Process of treating sulphur-bearing ores | |
| US3514281A (en) | Production of pyrite and/or sulfuric acid as by-product of copper smelting process | |
| US2055419A (en) | Recovery of sulphuric acid | |
| US1943336A (en) | Method of chloridizing sulphide ores | |
| US47497A (en) | Improved process for treating auriferous ores |