US899146A - Extraction of metals from their ores. - Google Patents
Extraction of metals from their ores. Download PDFInfo
- Publication number
- US899146A US899146A US29263205A US1905292632A US899146A US 899146 A US899146 A US 899146A US 29263205 A US29263205 A US 29263205A US 1905292632 A US1905292632 A US 1905292632A US 899146 A US899146 A US 899146A
- Authority
- US
- United States
- Prior art keywords
- ore
- solution
- gold
- alkali metal
- ores
- 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 20
- 239000002184 metal Substances 0.000 title description 20
- 150000002739 metals Chemical class 0.000 title description 17
- 238000000605 extraction Methods 0.000 title description 4
- 239000000243 solution Substances 0.000 description 40
- 239000002904 solvent Substances 0.000 description 31
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 21
- 239000010931 gold Substances 0.000 description 21
- 229910052737 gold Inorganic materials 0.000 description 21
- 229910052783 alkali metal Inorganic materials 0.000 description 19
- 150000001340 alkali metals Chemical class 0.000 description 19
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 238000000034 method Methods 0.000 description 14
- 230000008569 process Effects 0.000 description 14
- 229910002651 NO3 Inorganic materials 0.000 description 12
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 12
- 239000003610 charcoal Substances 0.000 description 12
- 230000001376 precipitating effect Effects 0.000 description 11
- 150000003839 salts Chemical class 0.000 description 10
- 238000001354 calcination Methods 0.000 description 5
- CVHZOJJKTDOEJC-UHFFFAOYSA-N saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 5
- 229940081974 saccharin Drugs 0.000 description 5
- 235000019204 saccharin Nutrition 0.000 description 5
- 239000000901 saccharin and its Na,K and Ca salt Substances 0.000 description 5
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 4
- 239000002956 ash Substances 0.000 description 4
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 238000007865 diluting Methods 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 229940072033 potash Drugs 0.000 description 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 3
- 235000015320 potassium carbonate Nutrition 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 235000010333 potassium nitrate Nutrition 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000009324 Pinus caribaea Nutrition 0.000 description 1
- 235000008568 Pinus coulteri Nutrition 0.000 description 1
- 244000083281 Pinus coulteri Species 0.000 description 1
- 235000017339 Pinus palustris Nutrition 0.000 description 1
- 235000007738 Pinus rigida Nutrition 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- LEHOTFFKMJEONL-UHFFFAOYSA-N Uric Acid Chemical compound N1C(=O)NC(=O)C2=C1NC(=O)N2 LEHOTFFKMJEONL-UHFFFAOYSA-N 0.000 description 1
- TVWHNULVHGKJHS-UHFFFAOYSA-N Uric acid Natural products N1C(=O)NC(=O)C2NC(=O)NC21 TVWHNULVHGKJHS-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229940116269 uric acid Drugs 0.000 description 1
- 239000002023 wood Substances 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
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/22—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
- C22B3/24—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition by adsorption on solid substances, e.g. by extraction with solid resins
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Definitions
- This invention has reference to the extraction of metals lioln ores.
- ltlthmzgh primarily designed for the treat' plicable. for the treatment of pyritie or nonpvritic ores.
- the invention relates particularly to the process of extracting the precious or ba e metals from the crushed or reduced ore by means ol a solvent s lution.
- the presemimprovements give, among others, the lollowing advantages, namelyz- They cnabie the xtraction of the metal to be ell'ected much m re expeditiously; a higher extraction is ohtaiaed, and the loss of line gold in slimes etcetera is entirely obviated.
- The. process is extr mely simple and pos- Sesses decided advantages both as regards handling and working, over the processt s at present in vogue.
- the ore, alter being crushed goes direct into the vats [or treatment with the solution; practically all the gold is extracted before the ore. leaves the vats; no slimcs are formed, and no further treatment of the tailings in any way is required.
- the gold extracted is much purer, and finally, the. initial cost of the installation of the plant is very considerably reduced.
- the essence of the present invention lies in the employment of a solvent solution eonsist-ing of sulfuric acid, salt (ehlorid of sodium), nitrate of an alkali metal (nitrate of soda or nit-rate of potash), permanganate of sodav or permanganate of potash, and water, with or without the addition of saecharin (C II O all in suitable quantities or proportions.
- saecharin C II O all in suitable quantities or proportions.
- the function of the saeeharin is that of an oxidizing agent.
- the ore as it comes from the mine is crushed or conn'ninut-ed, as for example by passing it through stone erushers or crushing rollers, or
- the vats or tanks shall be so constructed as to withstand the action of the solution; for example, the vats ma; be. made of pitchpine, and. with the. object of counteracting any action of the solvent which might cause shrinkage of the wood, the vats may be bound with iron bands which are anapt l to nmke thevats liquidtight to prevent leakages.
- vats may be built of bricks on a foundation of concrete and be lined with a suitable inm-perishable cement.
- all the utensils. pipes, pumps, ctcctera employed in the process, either for the cireulation or manipulation of the solvent, should be of vuleanite. glass. or other suitable anti-cm-rosive or acid resisting material.
- vats are preferably so arranged that the solution can he drawn on from the first into the next vat n! tank, and so on through the whole series, the solution being brought up to its original strength as it passes on from vat to vat. In this manner the solution can be so manipulated as to reduce the cost, in rotation, to one quarter that of the original solution.
- a certain quantity remains in the ore. This is preferably leached off with water, which. percolating or passing through the ore, carries with it all the auriferous fluid. This washing is preferably continued until the liquid passing from the vat is colorless. When this condition is reached the vatcan be discharged and re-cliargr-l with the ore for treatment.
- the solution extracts all metals from ores, it has the power of holding all these metals in solution as long as the standard strenglji is maintained.
- he ore may be treated with the solvent solution in any other suitable and convenient manner.
- i or each ton of ore treated I employ the several ingredients in the following quantities or proportions, namely:water 40 gallons or 400 pounds, sull'uric acid 80 pounds, salt (chlorid of sodium) 40 pounds, nitrate of an alkali metal (nitrate ol soda or nitrate of potash) 2 pounds, permanganate of soda or permanganate of potash 2 pounds.
- saccharin in addition to the permanganate of soda or permanganate of potash, saccharin mayoe employed and two pounds (more or less) be used in the production of the above quantity of the solvent.
- the quantities of the several ingredients may be varied as may be found necessary or desirable to suit the nature of the ore to be treated.
- the solvent solution maybe produced by mixing the several ingredients enumerated in any suitable and preferred manner.
- charcoal As a precipitant for recovering the gold from the aurit'erous lluid I prefer to employ charcoal, although any other suitable reagent may be used. By employing charcoal as the precipitant the gold is obtained in the metallic state, and all the baser metals are left in the lluid.
- the original solution becomes so highly charged or saturated with the gold and other metals that it can no longer be used for ell'ecting the extraction.
- it is finally drawn oil and very ireely diluted with water (say three to live parts of water to one of solution) and then passed through the charcoal.
- the dilution of the solution absolutely esseni ial. other wise, the solution, being too strong, would have a tendency to destroy the )recipitating power of the charcoal.
- the charcoal may be iuclosed in bags or covers made of muslin or other similar suitable material. I or ell'ecting the recovery of the gold from the charcoal the latter is burned in a suitable vessel, the ashes containing the gold being subsequently mixed with suitable fluxes and reduced in the ordinary manner.
- T he process of extracting metals from ores which consists in crushing the ore, then treating the crushed ore with a solvent solution of sulfuric acid, salt, nitrate of an alkali metal, and permanganate of an alkali metal, and water with the addition of sacr-harin, the ore being treated with the solvent by rotation, or so that thesolution can be drawn oil from the first vat into the next rat and so on through the whole series, the solution being brought up to its original strength as it passes on from vat to vat, and subsequently diluting the solvent solution with water reparatory to precipitating the gold there ii'om and finally precipitating the gold, substantially as described.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Extraction Or Liquid Replacement (AREA)
Description
ca t- 1 "ta UNITED ST; TES PATENT OFFICE.
JABEZ TURTON, OF JOHANXESBURG, TRAXSYAAL.
EXTRACTION OF ZYIETALS FBOIlI THEIR GEES.
Application filed December 20, 1905.
T0 (17 wit m1 it may concern:
Be it known that l, Jxmiz Tt'n'rox, a subject of the. liing of Great Britain, residing at Jrihannesbnrg. 'lransvaal, have invented certain new and usel'ul improvements iltelating to the l'ixtraction of Metals from Their ()res, of which the fol owing is a specilicz'ltion.
This invention has reference to the extraction of metals lioln ores.
ltlthmzgh primarily designed for the treat' plicable. for the treatment of pyritie or nonpvritic ores.
The invention relates particularly to the process of extracting the precious or ba e metals from the crushed or reduced ore by means ol a solvent s lution.
As comparul with certain pro esses heretol'ore proposed for the purposes specified, the presemimprovements give, among others, the lollowing advantages, namelyz- They cnabie the xtraction of the metal to be ell'ected much m re expeditiously; a higher extraction is ohtaiaed, and the loss of line gold in slimes etcetera is entirely obviated. The. process is extr mely simple and pos- Sesses decided advantages both as regards handling and working, over the processt s at present in vogue. The ore, alter being crushed, goes direct into the vats [or treatment with the solution; practically all the gold is extracted before the ore. leaves the vats; no slimcs are formed, and no further treatment of the tailings in any way is required. The gold extracted is much purer, and finally, the. initial cost of the installation of the plant is very considerably reduced.
The essence of the present invention lies in the employment of a solvent solution eonsist-ing of sulfuric acid, salt (ehlorid of sodium), nitrate of an alkali metal (nitrate of soda or nit-rate of potash), permanganate of sodav or permanganate of potash, and water, with or without the addition of saecharin (C II O all in suitable quantities or proportions. The function of the saeeharin is that of an oxidizing agent.
In carrying out the invention in the ease of ordinary conglomerate and non-pyritie ores, the ore as it comes from the mine is crushed or conn'ninut-ed, as for example by passing it through stone erushers or crushing rollers, or
Specification of Letters Patent.
1 nature of the. ore. placed in a vat or tank (or vats or tanks) of Patented Sept. 22. 1908.
Serial No. 292,632.
by any other suitable means, to reduce itto a suitable size to render it amenable to treatment by the. chemical solvent. The degree of eomminution will vary according to the The crushed ore is then any suitable Ctmstruction. As the s'vlvent solution 1s very penetrative, it is desirable that the vats or tanks shall be so constructed as to withstand the action of the solution; for example, the vats ma; be. made of pitchpine, and. with the. object of counteracting any action of the solvent which might cause shrinkage of the wood, the vats may be bound with iron bands which are anapte l to nmke thevats liquidtight to prevent leakages. if preferred the vats may be built of bricks on a foundation of concrete and be lined with a suitable inm-perishable cement. [t is also desirable that all the utensils. pipes, pumps, ctcctera employed in the process, either for the cireulation or manipulation of the solvent, should be of vuleanite. glass. or other suitable anti-cm-rosive or acid resisting material. After a sulii -ient quanlit of the ore has been placed in the tank, the solvent solution is then pumped on to the contents and allowed to pereolate through, and sutli cicnt time given for the ell'ective working of the solvent, after which it is treated as hereinafter explained for the purpose of extractin; the. metal.
I prefer to treat the re wit h the. solvent by IUlitliflll, that is to say the vats are preferably so arranged that the solution can he drawn on from the first into the next vat n! tank, and so on through the whole series, the solution being brought up to its original strength as it passes on from vat to vat. In this manner the solution can be so manipulated as to reduce the cost, in rotation, to one quarter that of the original solution. After the original solution has passed through the ore in a vat it will be understood that a certain quantity remains in the ore. This is preferably leached off with water, which. percolating or passing through the ore, carries with it all the auriferous fluid. This washing is preferably continued until the liquid passing from the vat is colorless. When this condition is reached the vatcan be discharged and re-cliargr-l with the ore for treatment.
Although the solution extracts all metals from ores, it has the power of holding all these metals in solution as long as the standard strenglji is maintained. he ore may be treated with the solvent solution in any other suitable and convenient manner. i or each ton of ore treated I employ the several ingredients in the following quantities or proportions, namely:water 40 gallons or 400 pounds, sull'uric acid 80 pounds, salt (chlorid of sodium) 40 pounds, nitrate of an alkali metal (nitrate ol soda or nitrate of potash) 2 pounds, permanganate of soda or permanganate of potash 2 pounds. in addition to the permanganate of soda or permanganate of potash, saccharin mayoe employed and two pounds (more or less) be used in the production of the above quantity of the solvent. The quantities of the several ingredients may be varied as may be found necessary or desirable to suit the nature of the ore to be treated. The solvent solution maybe produced by mixing the several ingredients enumerated in any suitable and preferred manner.
in the process of treating highly pyritic ores it is necessary to roast the ore in kilns. The ore -ed not be tincly comminuted as pieces ranging from one ounce to tour or live pounds in weight would be suitable for the roasting process. dead mast is preferable although not absolutely necessary; the ore must he rendered highly porous by calcination so that it is amenable to the penetrative action of the solvent solution. After the calcination oi the ore is completed, it. is crushed or comminuted' (more or less coarse and treated as before described with the solvent solution.
As a precipitant for recovering the gold from the aurit'erous lluid I prefer to employ charcoal, although any other suitable reagent may be used. By employing charcoal as the precipitant the gold is obtained in the metallic state, and all the baser metals are left in the lluid.
In course of time the original solution becomes so highly charged or saturated with the gold and other metals that it can no longer be used for ell'ecting the extraction. When this stage is reached it is finally drawn oil and very ireely diluted with water (say three to live parts of water to one of solution) and then passed through the charcoal. The dilution of the solution absolutely esseni ial. other wise, the solution, being too strong, would have a tendency to destroy the )recipitating power of the charcoal. The charcoal may be iuclosed in bags or covers made of muslin or other similar suitable material. I or ell'ecting the recovery of the gold from the charcoal the latter is burned in a suitable vessel, the ashes containing the gold being subsequently mixed with suitable fluxes and reduced in the ordinary manner.
What I claim as my invention and desire to protect by Letters Patent is:
1. The process of extracting metals from ore which consists in subjecting the ore to the action of a solvent solution of sulfuric acid, sodium chlorid a nitrate of an alkali metal, a permanganate of an alkali metal, saccharin and water, and subsequently precipitating the metal from said solution.
2. The process of extracting metals from ores which consists in crushing the ore, then treating the crushed ore with a solvent solution of sulfuric acid, salt, nitrate of an alkali metal, and permanganate ol' an alkali metal, with the addition oi saccharin and water, and subsequently precipitating the gold from said solution, substantially as described.
The process of extracting metals from ores which consisis in crushing the ore then treating the crushed ore with a solvent solution of sulfuric acid, salt, nitrate of an alkali metal and permanganate of an alkali metal, and water, with the addition of sacchurin, and subsequently precipitating the gold from the solvent solution on chart-mil, and then burning the charcoal and adding llux to the ashes and reducing same to recover the gold, substantially as described.
4. The process of treating pyritic ores for extracting metals therefrom, which consists in reducing the, ore to a suitable size, then roasting the same to render it porous, crushing it after calcination is completed, then treating the same with a solvent solution of sulfuric acid, salt, nitrate of an alkali metal and permanganate of an alkali metal, and water, with the addition of saceharin and subsequently precipitating the gold from the solvent solution, substantially as described.
5. The process of treating pyriticores for extracting metals therefrom, which consists in reducing the ore to a suitable size, then roasting the same to render it. porous, crushing it after calcination is completed, then treating the same with a solvent solution of sulfuric acid, salt, nitrate of an alkali metal, and permanganate of an alkali metal, and water, with the addition of saceharin, and subsequently precipitating the. gold from the solvent solution on charcoal, substan tially as described.
6. The process of treating pyritic ores for extracting metals therefrom, which consists in reducing the ore to a suitable size, then roasting the same to render it porous, crushing it after calcination is completed, then treating the same with a solvent solution of sulfuric acid, salt, nitrate of an alkali metal, and permanganate of an alkali metal, and water, with the addition of saccharin, and subsequently precipitating tht gold from the solvent solution on charcoal, and then burning the eharccal and adding ttux to the ashes and redu ing same to recover the gold, sobst antially as described.
7. The process of extracting metals from ores which consists in crushing the ore, then treating the crushed ore with a solvent solution of sulfuric a d, salt, nitrate of an alkali metal, and permanganate of an alkali metal, and water, with the addition of saceharin, and subsequently diluting the solvent solution with water preparatory to precipitating the gold therefrom and finally precipitating the gold, substantially as described.
T he process of extracting metals from ores which consists in crushing the ore, then treating the crushed ore with a solvent solution of sulfuric acid, salt, nitrate of an alkali metal, and permanganate of an alkali metal, and water with the addition of sacr-harin, the ore being treated with the solvent by rotation, or so that thesolution can be drawn oil from the first vat into the next rat and so on through the whole series, the solution being brought up to its original strength as it passes on from vat to vat, and subsequently diluting the solvent solution with water reparatory to precipitating the gold there ii'om and finally precipitating the gold, substantially as described.
The process of extracting metals from ores which consists in crushing the ore, then treating the crushed ore with a solvent solution consisting of eight Y pounds of sulfuric acid, forty pounds of salt, twenty two and a half pounds of nitrate of an alkali metal, two ounds permanganate of an alkali met: al, and tour hundred pounds of water, with two pounds of saccharin per ton of ore to be treated, the ore being treated with the solvent by rotation, then washing the ore in the vat until the liquid passing from the vat is colorless, then diluting the solvent solution with water, then precipitating the gold from the diluted solution on charcoal, then burning the charcoal, and then adding flux to the charcoal ashes and reducing the same to recover the gold, substantialtv as described.
In witness whereof I have hereunto set in hand in the presence of two subscribing witnesses.
JABEZ TURTON.
WVitnesses:
CHAS. OvExnaLE, It. OVENDALE.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US29263205A US899146A (en) | 1905-12-20 | 1905-12-20 | Extraction of metals from their ores. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US29263205A US899146A (en) | 1905-12-20 | 1905-12-20 | Extraction of metals from their ores. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US899146A true US899146A (en) | 1908-09-22 |
Family
ID=2967571
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US29263205A Expired - Lifetime US899146A (en) | 1905-12-20 | 1905-12-20 | Extraction of metals from their ores. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US899146A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| USB369379I5 (en) * | 1973-06-12 | 1976-03-30 | ||
| US5096486A (en) * | 1990-12-13 | 1992-03-17 | Sunshine Precious Metals Incorporated | Treatment of metal bearing mineral material |
-
1905
- 1905-12-20 US US29263205A patent/US899146A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| USB369379I5 (en) * | 1973-06-12 | 1976-03-30 | ||
| US4013754A (en) * | 1973-06-12 | 1977-03-22 | Continental Oil Company | Static leaching copper ore |
| US5096486A (en) * | 1990-12-13 | 1992-03-17 | Sunshine Precious Metals Incorporated | Treatment of metal bearing mineral material |
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