US1236501A - Process of extracting precious metals and other metals from ore. - Google Patents
Process of extracting precious metals and other metals from ore. Download PDFInfo
- Publication number
- US1236501A US1236501A US13863116A US13863116A US1236501A US 1236501 A US1236501 A US 1236501A US 13863116 A US13863116 A US 13863116A US 13863116 A US13863116 A US 13863116A US 1236501 A US1236501 A US 1236501A
- Authority
- US
- United States
- Prior art keywords
- ore
- cyanid
- metals
- solution
- oil
- 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 17
- 239000010970 precious metal Substances 0.000 title description 5
- 239000002184 metal Substances 0.000 title description 2
- 229910052751 metal Inorganic materials 0.000 title description 2
- 150000002739 metals Chemical class 0.000 title description 2
- 238000005188 flotation Methods 0.000 description 16
- 239000000203 mixture Substances 0.000 description 14
- 239000003513 alkali Substances 0.000 description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229910052500 inorganic mineral Inorganic materials 0.000 description 6
- 239000011707 mineral Substances 0.000 description 6
- 235000010755 mineral Nutrition 0.000 description 6
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 5
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 5
- 229910052737 gold Inorganic materials 0.000 description 5
- 239000010931 gold Substances 0.000 description 5
- 229910052709 silver Inorganic materials 0.000 description 5
- 239000004332 silver Substances 0.000 description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 3
- 238000013019 agitation Methods 0.000 description 3
- 230000001804 emulsifying effect Effects 0.000 description 3
- 239000011701 zinc Substances 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000013528 metallic particle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002562 thickening agent 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
- C22B11/00—Obtaining noble metals
- C22B11/08—Obtaining noble metals by cyaniding
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S209/00—Classifying, separating, and assorting solids
- Y10S209/901—Froth flotation; copper
Definitions
- This invention relates to a process for the treatment of'the ores of the precious metals (gold and silver) and has for its object the extraction of as large a proportion as possible of the precious metals contained in the ore and at the same time recovering any'base metals, such as copper, lead, zinc, iron, etc., which may be present in the ore.
- alkali or a mixture of alkalis is added to the ore.
- the amount of alkali depends upon the acidity of-the ore under treatment. It willvary from one-half Specification of Letters Patent.
- a suitable flotation oil the amount of which may vary from onehalf pound to four pounds per ton .of ore.
- the ore, the cyanid solution, the alkalis and'the oil are mixed together in the grinding mill.
- the oil emulsifies during v the grinding and coats the sulfids and metallic
- the mixture is drawn from the mill and additional cyanid solution of the same strength previously used is added, Tnaking the ratio of ore to solution one to three or one to four.
- ture is'then flowed to a flotation cell, such as the Callow pneumatic cell or the minerals separation cell, where a large portion of the richest and finest minerals, including both sulfids and metallic particles, are floated by the gas'bubbles produced in the mixture in the flotation cell and removed from the pulp as a concentrate.
- the minerals recovered by fine that table concentration cannot save them.
- These concentrates are very diflicult to treat in the cyanid solution if not removed. 7
- the tailings from the concentration tables pass intothickening tanks of the Dorr
- the clear solution overflowing from thethickening tanks is treated with zinc to precipitate the gold and silver in the usual manner.
- the underflow from the thickeners, containing the pulp, flows toagitating tanks'of the sort usually used in connection with the cyanid process. After agitation,
- the mixthe pulp may be passed through any recognized type of slime filter to remove the gold and silver solution from the ore.
- the so lution is then treated with zinc to precipitate the gold and silver contained in it.
- flotation oil be added to the ore before the ore enters the grinding mill. It may be added after the ore has been finely ground and emulsified by agitation, either in a mechanical oil flotation cell, or an agitation tank before reaching the flotation cell.
- An improvement in the cyanid process for treating ores comprising the step of separating out a portion of the values in the ore by flotation in the presence of the cyanid solution.
- An improvement in the cyanid process for the treatment of ores comprising mixing the ore with cyanid solution and oil and alkali; emulsifying the oil in the presence of the ore, the alkali, and the cyanid solution; floating a portion of the values in the pulp by producing gas bubbles in the mixture, and removing the values floated.
- An improvement in the cyanid process of treating ores comprising mixing the are with an equal or greater amount of'cyanid solution, alkali sufiicient in quantity to counteract the acidity of the ore, and a quantity of oil amounting to a fraction of one per cent. of the ore; emulsifying the oil in the presence of the ore, the alkali and the cyanid solution; and producing gas bubbles in the mixture whereby a portion of the values are floated.
- An improvement in the cyanid of treating ores comprising mixing the ore with cyanid solution and oil, and flowing the resulting mixture to a grinding mill, and then to a flotation cell.
- An improvement in the cyanid process of treating ores comprising mixing the ore with an 'equal quantity of cyanid solution, alkali sufficient to counteract the acidity of the ore, and an amount of oil equal to a fraction of one per cent. of the ore; passing the resulting mixture through a grinding mil-l; adding additional cyanid solution;
- a process for the treatment of ores comprising mixing the ore with c anid solution an oil, emulsifying the oi, passing the "mixture through a flotation cell Where a portion of the minerals are separated out and removed, passing the remaining mixture I over concentratin tables Where a further portion of the minerals are separated out, separating the solids remaining in the mixture from the solution, and precipitating the values dissolved in the solution.
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
UNITEDTATES PATENT OFFICE.
JOHN M. TIPPETT, OF COLORADO SPRINGS, COLORADO.
PROCESS OF EXTRACTING PRECIOUS METALS AND OTHER METALS FROM ORE.
No Drawing.
lowing is a specification.
This invention relates to a process for the treatment of'the ores of the precious metals (gold and silver) and has for its object the extraction of as large a proportion as possible of the precious metals contained in the ore and at the same time recovering any'base metals, such as copper, lead, zinc, iron, etc., Which may be present in the ore.
I have discovered that by following the procedure hereinafter'detailed, it is possible to accomplish oil flotation in a cyanid solution. By combining oil flotation with the. steps of the cyanid process, I have pro- 'duced a process of extracting which is more efficient and also more economical than previous methods of treating the ores of precious metals. The process is applicable to any gold or silver ores, and is particularly adapted to the treatment of ores from the Cripple Creek district in Teller county, Colorado.
In order that my invention may clearly be understood, I shall proceed to describe in detail a specific embodiment of it, as well as some modifications of the embodiment first described. It should be clearly understood, however, that my invention is by no of water. The ore and cyanid solution are then fed to a tube mill,-a.ball mill, a Chilian mill, or stamp, where the ore is finely com-- minuted.
While the ore andthe cyanid solution are passing into the mill an alkali or a mixture of alkalis is added to the ore. The amount of alkali depends upon the acidity of-the ore under treatment. It willvary from one-half Specification of Letters Patent.
particles present.
type.
Patented Aug. 14, 1917.
Application filed December 23, 1916. Serial No. 138,631.
pound to ten pounds per ton of ore. It is not necessary that any particular alkali be used, although I have found caustic soda (NaOH) preferable. Sodium carbonate (Na CO ),"or lime (CaO), or a mixture of the three alkalis mentioned, or any two of them, is satisfactory. The adding of the alkaliv or alkalis serves two purposes: It preventsthe cyanid from being consumed should the pulp become too acid on account of the acidity of the ore, and I have foundv it is of material assistance in effecting fio tation. I
As the ore and cyanidso-lution enter into the mill, I add a suitable flotation oil, the amount of which may vary from onehalf pound to four pounds per ton .of ore.
The ore, the cyanid solution, the alkalis and'the oil are mixed together in the grinding mill. The oil emulsifies during v the grinding and coats the sulfids and metallic After the grinding has reduced the ore to the degree of fineness usual for cyanid treatment, the mixture is drawn from the mill and additional cyanid solution of the same strength previously used is added, Tnaking the ratio of ore to solution one to three or one to four. ture is'then flowed to a flotation cell, such as the Callow pneumatic cell or the minerals separation cell, where a large portion of the richest and finest minerals, including both sulfids and metallic particles, are floated by the gas'bubbles produced in the mixture in the flotation cell and removed from the pulp as a concentrate. The minerals recovered by fine that table concentration cannot save them. These concentrates are very diflicult to treat in the cyanid solution if not removed. 7
I The tailings from the flotation cell are passed over gravity concentration tables, which may be of the well known Wilfley type. There the coarser particles-of mineral which flotation failed to recover are separated from the pulp.
The tailings from the concentration tables pass intothickening tanks of the Dorr The clear solution overflowing from thethickening tanks is treated with zinc to precipitate the gold and silver in the usual manner. The underflow from the thickeners, containing the pulp, flows toagitating tanks'of the sort usually used in connection with the cyanid process. After agitation,
The mixthe pulp may be passed through any recognized type of slime filter to remove the gold and silver solution from the ore. The so lution is then treated with zinc to precipitate the gold and silver contained in it.
Changes may be made in the details of the process described Without departing from my invention. For example, it is not necessary that the flotation oil be added to the ore before the ore enters the grinding mill. It may be added after the ore has been finely ground and emulsified by agitation, either in a mechanical oil flotation cell, or an agitation tank before reaching the flotation cell.
I claim as my invention 1. An improvement in the cyanid process for treating ores, comprising the step of separating out a portion of the values in the ore by flotation in the presence of the cyanid solution.
2. An improvement in the cyanid process for the treatment of ores, comprising mixing the ore with cyanid solution and oil,
and separating a portion of the values from the mixture by flotation.
3. An improvement in the cyanid process for the treatment of ores, comprising mixing the ore with cyanid solution and oil and alkali; emulsifying the oil in the presence of the ore, the alkali, and the cyanid solution; floating a portion of the values in the pulp by producing gas bubbles in the mixture, and removing the values floated.
4. An improvement in the cyanid process of treating ores, comprising mixing the are with an equal or greater amount of'cyanid solution, alkali sufiicient in quantity to counteract the acidity of the ore, and a quantity of oil amounting to a fraction of one per cent. of the ore; emulsifying the oil in the presence of the ore, the alkali and the cyanid solution; and producing gas bubbles in the mixture whereby a portion of the values are floated.
5. An improvement in the cyanid of treating ores, comprising mixing the ore with cyanid solution and oil, and flowing the resulting mixture to a grinding mill, and then to a flotation cell.
6. An improvement in the cyanid process of treating ores, com-prising mixing cyanid solution, oil, and alkali with the ore; and passing the resulting mixture to a grinding mill, and then to a flotation cell.
7. An improvement in the cyanid process of treating ores, comprising mixing the ore with an 'equal quantity of cyanid solution, alkali sufficient to counteract the acidity of the ore, and an amount of oil equal to a fraction of one per cent. of the ore; passing the resulting mixture through a grinding mil-l; adding additional cyanid solution;
and passing the mixture to a flotation cell.
8. A process for the treatment of ores, comprisin mixing the ore with c anid solution an oil, emulsifying the oi, passing the "mixture through a flotation cell Where a portion of the minerals are separated out and removed, passing the remaining mixture I over concentratin tables Where a further portion of the minerals are separated out, separating the solids remaining in the mixture from the solution, and precipitating the values dissolved in the solution.
JOHN M. TIP-PETT.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13863116A US1236501A (en) | 1916-12-23 | 1916-12-23 | Process of extracting precious metals and other metals from ore. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13863116A US1236501A (en) | 1916-12-23 | 1916-12-23 | Process of extracting precious metals and other metals from ore. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1236501A true US1236501A (en) | 1917-08-14 |
Family
ID=3304322
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US13863116A Expired - Lifetime US1236501A (en) | 1916-12-23 | 1916-12-23 | Process of extracting precious metals and other metals from ore. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1236501A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3964997A (en) * | 1973-10-24 | 1976-06-22 | David Weston | Concentration of gold, sulphide minerals and uranium oxide minerals by flotation from ores and metallurgical plant products |
| US4384889A (en) * | 1981-04-15 | 1983-05-24 | Freeport Research & Development Company | Simultaneous leaching and cementation of precious metals |
-
1916
- 1916-12-23 US US13863116A patent/US1236501A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3964997A (en) * | 1973-10-24 | 1976-06-22 | David Weston | Concentration of gold, sulphide minerals and uranium oxide minerals by flotation from ores and metallurgical plant products |
| US4384889A (en) * | 1981-04-15 | 1983-05-24 | Freeport Research & Development Company | Simultaneous leaching and cementation of precious metals |
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