US504109A - Juan francisco nepomuceno macay - Google Patents
Juan francisco nepomuceno macay Download PDFInfo
- Publication number
- US504109A US504109A US504109DA US504109A US 504109 A US504109 A US 504109A US 504109D A US504109D A US 504109DA US 504109 A US504109 A US 504109A
- Authority
- US
- United States
- Prior art keywords
- chloride
- silver
- sodium
- solution
- macay
- 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
- ORTQZVOHEJQUHG-UHFFFAOYSA-L Copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 68
- BQCADISMDOOEFD-UHFFFAOYSA-N silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 58
- 229910052709 silver Inorganic materials 0.000 description 56
- 239000004332 silver Substances 0.000 description 56
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 52
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 36
- 239000011734 sodium Substances 0.000 description 36
- 229910052708 sodium Inorganic materials 0.000 description 36
- 229960003280 cupric chloride Drugs 0.000 description 34
- 238000009835 boiling Methods 0.000 description 18
- UCKMPCXJQFINFW-UHFFFAOYSA-N sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 18
- 238000000034 method Methods 0.000 description 16
- 239000007788 liquid Substances 0.000 description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 8
- 239000003153 chemical reaction reagent Substances 0.000 description 8
- 238000001816 cooling Methods 0.000 description 8
- NMCUIPGRVMDVDB-UHFFFAOYSA-L Iron(II) chloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 6
- 238000003801 milling Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- OXBLHERUFWYNTN-UHFFFAOYSA-M Copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 4
- BAUYGSIQEAFULO-UHFFFAOYSA-L Iron(II) sulfate Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 4
- RBTARNINKXHZNM-UHFFFAOYSA-K Iron(III) chloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 4
- JEIPFZHSYJVQDO-UHFFFAOYSA-N Iron(III) oxide Chemical compound O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 229940045803 cuprous chloride Drugs 0.000 description 4
- 229960002089 ferrous chloride Drugs 0.000 description 4
- 235000003891 ferrous sulphate Nutrition 0.000 description 4
- 239000011790 ferrous sulphate Substances 0.000 description 4
- 229910000460 iron oxide Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- PMZURENOXWZQFD-UHFFFAOYSA-L na2so4 Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 4
- 230000001590 oxidative Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000001117 sulphuric acid Substances 0.000 description 4
- 235000011149 sulphuric acid Nutrition 0.000 description 4
- 241000132007 Bahia Species 0.000 description 2
- AQMRBJNRFUQADD-UHFFFAOYSA-N Copper(I) sulfide Chemical compound [S-2].[Cu+].[Cu+] AQMRBJNRFUQADD-UHFFFAOYSA-N 0.000 description 2
- RCJVRSBWZCNNQT-UHFFFAOYSA-N Dichlorine monoxide Chemical compound ClOCl RCJVRSBWZCNNQT-UHFFFAOYSA-N 0.000 description 2
- 229920002456 HOTAIR Polymers 0.000 description 2
- 235000017858 Laurus nobilis Nutrition 0.000 description 2
- 206010033799 Paralysis Diseases 0.000 description 2
- AKHNMLFCWUSKQB-UHFFFAOYSA-L Sodium thiosulphate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 2
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 2
- 229910052787 antimony Inorganic materials 0.000 description 2
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 2
- 229910052785 arsenic Inorganic materials 0.000 description 2
- 125000004429 atoms Chemical group 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000320 mechanical mixture Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 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
- 235000019345 sodium thiosulphate Nutrition 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- PGWMQVQLSMAHHO-UHFFFAOYSA-N sulfanylidenesilver Chemical class [Ag]=S PGWMQVQLSMAHHO-UHFFFAOYSA-N 0.000 description 2
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
- C22B11/04—Obtaining noble metals by wet processes
Definitions
- My invention relates to an improved process for extracting silver from free milling ores without roasting, or from rebellious ores after they have been submitted to an oxidizing roasting, and my improved process is not only available for the treatment of rich ores but for the economical treatment of low grade ores and ores which heretofore could not by well known processes be worked economically.
- solution contains cupric chloride and chloride of sodium, there being for each part by weight of metallic silverin the ore eightysix minimum to one hundred and fifty maximum parts by weight of cupric chloride and from four hundred and twenty-four'minimurn to five hundred and fifty maximum parts by weight of chloride or sodium, these ingredients being dissolved in a quantity of water about three and one tenth (3.1) times greater than their mass by weight.
- chloride of sodium in solution is to dissolve the argentic chloride first formed and to present anew clean surface of metallic silver, sulphide of silver or oxide of silver as the case may be, to the chloridizing action of the cupric chloride and cuprous chloride until the whole of the silver present has been converted into argentic chloride, and it is absolutely necessary that an excess of cupric chloride and chloride of sodium be employed to chloridize and dissolve each atom or quantity of metallic silver. Otherwise the chloridizingaction will be paralyzed by the formation on the silver particles of a layer of argentic chloride which will prevent the action of the cupric chloride.
- cuprous chloride in the presence of the oxygen of the air is converted first into cupric oxychloride, and this in the nascent state whether in the presence first of hydrochloric acid, or second, of ferrous chloride, or third of ferric chloride, or fourth, of ferrous sulphate and chloride of sodium, or fifth, of sulphuric acid and chloride of sodium, by a mutual exchange of elements is converted in the first case into the cupric chloride and water, and in the second and third cases, into cupric chloride and hydrated ferric oxide, and in the fourth case into cupric chloride (Gu01,) hydrated ferric oxide and sulphate of soda, or in the fifth case, into (OuOl,) cupric chloride, sulphate of soda and water.
- liquid A which carries in solution cupric chloride, chloride of sodium and some argentic chloride.
- This liquid A after each operation may be used again to treat new batches of ore ad infinitum, if from time to time thesmall mechanical loss of cupric chloride and chloride of sodium that takes place during each operation is replaced by adding from time to time a small additional quantity of these reagents.
- the further treatment of the solid matter containing the argentic chloride is conducted in Macays rotary filter by a cold dilute solution of hyposulphite of soda and the precipitation of the silver as sulphide of silver from such solution by an alkaline sulphide and the reduction of sulphide of silver to metallic silver are effected by well known processes for such purposes, the same however forming no essential feature of my present invention.
- I claim as my invention- The method of extracting silver from ores, which consists in subjecting the ore toa solution of cupric chloride with excess of chloride of sodium in substantially the proportion, by Weight, of eighty six parts of cupric chloride, and four hundred and twenty-four parts of chloride of sodium to each one part of native silver, or silver in the state of sulphide of silver, for the purposes set forth.
Description
UNITED STATES PATENT OFFICE.
JUAN FRANCISCO NEPOMUOENO MACAY, OECI-IARAPOTO, ECUADOR.
METHOD OF EXTRACTING SILVER FROM ORES.
SPECIFICATION forming part of Letters Patent No. 504,109, dated August 29, 1893.
Application filed May 1'7, 1888. Serial No. 274.227. (No specimens.)
To all whom it may concern.-
Be it known that I, J UAN FRANCISCO NE POMUCENO MACAY, of Charapoto, in the Republic of Ecuador, South America, and at present residing at Bahia de Oaraquez, Ecuador, have invented new and useful Improvements in Processes of Extracting Silver from Ores, of which the following is a full, clear, and exact description.
My invention relates to an improved process for extracting silver from free milling ores without roasting, or from rebellious ores after they have been submitted to an oxidizing roasting, and my improved process is not only available for the treatment of rich ores but for the economical treatment of low grade ores and ores which heretofore could not by well known processes be worked economically.
In treating silver sulphides with cupric chloride and chloride of sodium in solution, I have found in practice that in the methods heretofore known, owing to the insufficient amount of chloride of sodium, the chloridized silver forms a coating on the particles of ore and prevents the further action on the solphide of silver; hence considerable loss arises by the imperfect character of the operation. I have discovered that when an excess of chloride ofsodium is made use of, with the cupric chloride, in about the proportions hereinafter specified, the chloridized silver is taken up in solution as fast as it is formed until the whole of the silver is dissolved. By my improved process it is possible to extract from about 98 to 98.5 per cent. of the silver from raw free milling ores when this is present in the free state as native silver, sulphide of silver or oxide of silver and also to extract a high percentage of silver from raw free milling ores when they carry some sulphide of antimony, sulphide of arsenic, sulphide of lead or sulphide of copper either in chemical combination or in mechanical mixture, and also to extract a higher percentage of silver from rebellious ores after they have been submitted to an oxidizing roasting.
In the carrying out of myimproved process I may employ any desired character of apparatus (not to be acted upon by the reagents employed) suitable for the stages of the process, but as the same forms no necessary part mix a solution slightly less than saturated,
which solution contains cupric chloride and chloride of sodium, there being for each part by weight of metallic silverin the ore eightysix minimum to one hundred and fifty maximum parts by weight of cupric chloride and from four hundred and twenty-four'minimurn to five hundred and fifty maximum parts by weight of chloride or sodium, these ingredients being dissolved in a quantity of water about three and one tenth (3.1) times greater than their mass by weight. I would remark that while about eighty-six parts of cupric chloride and about four hundred and twenty-four parts of chloride of sodium are necessary as a minimum quantity to chloridize and dis solve or take up about one part by weight of metallic siiver,*I desire and prefer to have a slight excess of these dissolving and chloridizing-agents so as to make sure of the proper reactions. The quantity of ore and of the solution of oupric chloride and' chloride of sodium in the relative proportions just stated are brought together in a suitable vessel (not metallic) and are boiled with hot air or super-heated or live steam from two to four hours, in which time the silver will have been completely chloridized and dissolved, the heat of the boiling liquid making it possible for the chloride of sodium in solution to take up almost twice as much chloride of silver than if the solution acted when cold.
The action of chloride of sodium in solution is to dissolve the argentic chloride first formed and to present anew clean surface of metallic silver, sulphide of silver or oxide of silver as the case may be, to the chloridizing action of the cupric chloride and cuprous chloride until the whole of the silver present has been converted into argentic chloride, and it is absolutely necessary that an excess of cupric chloride and chloride of sodium be employed to chloridize and dissolve each atom or quantity of metallic silver. Otherwise the chloridizingaction will be paralyzed by the formation on the silver particles of a layer of argentic chloride which will prevent the action of the cupric chloride. Five minutes more or less before the boiling of the reagents with the ore is finished, I add to the contents of the tub a certain quantity (to be determined in the laboratory) of hydrochloric acid, or instead of it a certain quantity of ferrous chloride (FeOl,) or ferric chloride (Fefil or instead of any of the above named reagents there may be used ferrous sulphate (FeSOflO II,) and chloride of sodium or sulphuric acid and chloride of sodium. I then allow the materials to cool and stand about eighteen to twentyfour hours, exposed to the atmosphere. During the cooling of the contents of the boiling tub, the cuprous chloride in the presence of the oxygen of the air is converted first into cupric oxychloride, and this in the nascent state whether in the presence first of hydrochloric acid, or second, of ferrous chloride, or third of ferric chloride, or fourth, of ferrous sulphate and chloride of sodium, or fifth, of sulphuric acid and chloride of sodium, by a mutual exchange of elements is converted in the first case into the cupric chloride and water, and in the second and third cases, into cupric chloride and hydrated ferric oxide, and in the fourth case into cupric chloride (Gu01,) hydrated ferric oxide and sulphate of soda, or in the fifth case, into (OuOl,) cupric chloride, sulphate of soda and water. During the cooling of the liquid about one half of the argentic chlorido held in solution by the boiling liquid will have been precipitated on the ore. After cooling the liquid contents of the boiling tub are decanted and this is called liquid A which carries in solution cupric chloride, chloride of sodium and some argentic chloride. This liquid A after each operation may be used again to treat new batches of ore ad infinitum, if from time to time thesmall mechanical loss of cupric chloride and chloride of sodium that takes place during each operation is replaced by adding from time to time a small additional quantity of these reagents. The solid matter and the argentic chloride remaining in the boiling tub after the boiling and cooling operations and after the liquid A has been drawn 0d are put into Macays rotary decanting filter (I here make reference to my appa' ratus patented October 25, 1881, No. 248,768, for the device that I term Macays rotary decanting filter) and are washed with water to extract the cupric chloride and chloride of sodium, that may remain with the solid matter, and this solution is filtered and is added to the solution A and serves to replace in volume the water evaporated by the boiling operation and this solution is employed for future mixing and for chloridizing each new batch of the pulverized oreso that. the operations just named may be continuously repeated. The further treatment of the solid matter containing the argentic chloride is conducted in Macays rotary filter by a cold dilute solution of hyposulphite of soda and the precipitation of the silver as sulphide of silver from such solution by an alkaline sulphide and the reduction of sulphide of silver to metallic silver are effected by well known processes for such purposes, the same however forming no essential feature of my present invention.
I claim as my invention- The method of extracting silver from ores, which consists in subjecting the ore toa solution of cupric chloride with excess of chloride of sodium in substantially the proportion, by Weight, of eighty six parts of cupric chloride, and four hundred and twenty-four parts of chloride of sodium to each one part of native silver, or silver in the state of sulphide of silver, for the purposes set forth.
In witness whereof I hereunto set my hand in presence of two witnesses.
JUAN FRANCISCO NEPOMUCENO MAOAY.
Witnesses:
F. Canon, P. LORGE GOMEZ.
Publications (1)
Publication Number | Publication Date |
---|---|
US504109A true US504109A (en) | 1893-08-29 |
Family
ID=2572947
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US504109D Expired - Lifetime US504109A (en) | Juan francisco nepomuceno macay |
Country Status (1)
Country | Link |
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US (1) | US504109A (en) |
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- US US504109D patent/US504109A/en not_active Expired - Lifetime
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