US828288A - Process of silver extraction. - Google Patents
Process of silver extraction. Download PDFInfo
- Publication number
- US828288A US828288A US292555A US1905292555A US828288A US 828288 A US828288 A US 828288A US 292555 A US292555 A US 292555A US 1905292555 A US1905292555 A US 1905292555A US 828288 A US828288 A US 828288A
- Authority
- US
- United States
- Prior art keywords
- silver
- cyanid
- potassium
- solution
- 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
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 title description 25
- 229910052709 silver Inorganic materials 0.000 title description 25
- 239000004332 silver Substances 0.000 title description 25
- 238000000034 method Methods 0.000 title description 16
- 238000000605 extraction Methods 0.000 title description 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 12
- 229910052700 potassium Inorganic materials 0.000 description 12
- 239000011591 potassium Substances 0.000 description 12
- VRWKTAYJTKRVCU-UHFFFAOYSA-N iron(6+);hexacyanide Chemical compound [Fe+6].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] VRWKTAYJTKRVCU-UHFFFAOYSA-N 0.000 description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 6
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 6
- 229910052753 mercury Inorganic materials 0.000 description 6
- 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
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 239000003513 alkali 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
- 235000011118 potassium hydroxide Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical compound N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- NNFCIKHAZHQZJG-UHFFFAOYSA-N potassium cyanide Chemical compound [K+].N#[C-] NNFCIKHAZHQZJG-UHFFFAOYSA-N 0.000 description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 210000003050 axon Anatomy 0.000 description 1
- RCTYPNKXASFOBE-UHFFFAOYSA-M chloromercury Chemical compound [Hg]Cl RCTYPNKXASFOBE-UHFFFAOYSA-M 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- LWJROJCJINYWOX-UHFFFAOYSA-L mercury dichloride Chemical compound Cl[Hg]Cl LWJROJCJINYWOX-UHFFFAOYSA-L 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- PGWMQVQLSMAHHO-UHFFFAOYSA-N sulfanylidenesilver Chemical compound [Ag]=S PGWMQVQLSMAHHO-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
Definitions
- My. present invention consists of an improved process for extracting silver from its ores, and particularly from ores in which the silver'is present in combination with sulfur. Sulfur being present in almost all silver ores, the improved process is of very general application.
- the process consists of treating the orcs after such preliminary sizing as may be desired with a solution containing a mercurous potassic cyanid.
- This salt the characteristics of which are de-. scribed in my previous application, Serial No. 270,300, filed July 18, 1905, of which the present case is a division, has a selective affinity for silver in combination with sulfur. This selective aflinity I have demonstrated experimentally a great many times.
- the formula of the salt is KHgOy It forms with silver, when in combination with sulfur, a double saltthe cyanid of silver and potassium-which is freely soluble water, and also the sulfid of mercury, which is substantially insoluble in water and passes off with the tailings.
- ree oxygen in solution is necessary to dissolve silver or gold and form the double salt of potassium and silver or gold with cyanogen.
- mercurous potassic-cyanid may be produced in any desired way, since the particular method of its production does not seem to affect the results.
- I may, for example, add mercurous chlorid (Hg,Cl to a solution of potassium cyanid, (KCy.)
- the most suitable strength of the solution is to some extent dependent upon the silver content of the ore and the form in which the metal is present. I have obtained good results with solutions varying from .05 to .50 per cent.
- the metal may be separated from the solution in any of the approved methods commonly employed in cyanid processes, such as precipitation by zinc dust or shavings or electrolysis.
- the solution should be kept alkaline, and this may be effected by the addition of any suitable alkali, such as caustic potash or soda, although in most cases lime will be found to be not only the cheapest, but the best alkali.
- any suitable alkali such as caustic potash or soda
- lime will be found to be not only the cheapest, but the best alkali.
- This application is restricted to that form of my invention in which the mercurous potassic cyanid is formed by the addition of mercuric chlorid to a solution containing ferrocyanid.
- the other methods of obtaining the solvent, mercurous potassic cyanid are intended to be broadly covered by my application Serial N 0. 292,554, filed December 20, 1905, which is a division of the parent case, Serial No. 27 0,300, hereinbefore referred to.
- the rocess of extracting silver from its ores, 'Whic consists of adding to a mill solution containing cyanid and ferrocyanid of potash, a mercuric chlorid.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Description
UNITED STATES PATENT OFFICE.
FRANCIS J. HOBSON, OF GIIANAJUATO, MEXICO. PROCESS OF SILVER EXTRACTION.
Specification of Letters Patent.
Patented Aug. 7, 1906.
Original application filed July 18,1905, Serial No. 270,300. Divided and this application filed December 20, 1905. Serial No. 292,555.
To all whom it may concern:
Be it known that I, FRANCIS J. HOBSON, a citizen of the United States, now residing at Guanajuato, in the Republic of Mexico, have invented certain new and useful Improvements in Processes of Silver Extraction, of which the following is a specification.
My. present invention consists of an improved process for extracting silver from its ores, and particularly from ores in which the silver'is present in combination with sulfur. Sulfur being present in almost all silver ores, the improved process is of very general application.
Briefly outlined, the process consists of treating the orcs after such preliminary sizing as may be desired with a solution containing a mercurous potassic cyanid. This salt, the characteristics of which are de-. scribed in my previous application, Serial No. 270,300, filed July 18, 1905, of which the present case is a division, has a selective affinity for silver in combination with sulfur. This selective aflinity I have demonstrated experimentally a great many times. The formula of the salt is KHgOy It forms with silver, when in combination with sulfur, a double saltthe cyanid of silver and potassium-which is freely soluble water, and also the sulfid of mercury, which is substantially insoluble in water and passes off with the tailings. The reaction to which I here refer is expressed verbally as follows: Silver sulfid plus mercurous potassic cyanid e uals cyanid of silver and potassium plus suliid of mercury, and in chemical symbols the reaction is expressed thus:
AgS KHgCy KAgCy HgS.
The solvent which I employ in my improved process does not attack gold in any of the forms in which it appears to exist in ore, and although it forms the same salt of silver and potassium in solution as cyanid of potassium when the latter dissolves silver it does not do so in the same way, since potassium cyanid dissolves silver by the well-known Elsners equation, stated verbally as follows: Silver plus cyanid of potassium plus oxygen plus water equals cyanid of potassium and silver plus potassium hydrate or caustic potash. This equation in chemical symbols is stated thus:
2Ag 4K0y o H2O axA c axon.
The same equation applies to the solution of gold, gold replacing silver in it.
ree oxygen in solution is necessary to dissolve silver or gold and form the double salt of potassium and silver or gold with cyanogen.
may produce the mercurous potassic-cyanid in any desired way, since the particular method of its production does not seem to affect the results. I may, for example, add mercurous chlorid (Hg,Cl to a solution of potassium cyanid, (KCy.)
Another method which I may use is to add mercuric chlorid (corrosive sublimate, HgCl to the ordinary mill cyanid solutions containing ferrocyanid of potassium, in which case the reaction may be stated verbally thus: Ferrocyanid of potassium plus mercuric chlorid equals ferrocyanid of mercury plus chlorid of potassium. This reaction may be expressed in chemical symbols as follows:
This is succeeded by the following reaction: Ferrocyanid of mercury plus cyanid of potassium equals ferrocyanid of mercury and potassium plus mercurous potassic cyanid. This reaction. may oe expressed in chemical symbols as follows:
The most suitable strength of the solution is to some extent dependent upon the silver content of the ore and the form in which the metal is present. I have obtained good results with solutions varying from .05 to .50 per cent. The metal may be separated from the solution in any of the approved methods commonly employed in cyanid processes, such as precipitation by zinc dust or shavings or electrolysis.
The solution should be kept alkaline, and this may be effected by the addition of any suitable alkali, such as caustic potash or soda, although in most cases lime will be found to be not only the cheapest, but the best alkali. This application is restricted to that form of my invention in which the mercurous potassic cyanid is formed by the addition of mercuric chlorid to a solution containing ferrocyanid. The other methods of obtaining the solvent, mercurous potassic cyanid, are intended to be broadly covered by my application Serial N 0. 292,554, filed December 20, 1905, which is a division of the parent case, Serial No. 27 0,300, hereinbefore referred to.
Having thus described my invention, What I claim, and Wish to protect by Letters Patent of the United States, is-
1. The process of extracting silver from its ores, which consists of subjecting the ores to the action of a solution of cyanid and ferrocyanid of an alkaline metal, to which has been added mercuric chlorid.
2. The process of extracting silver from its ores, Which consists of subjecting the ores to the action of a solution of ferrocyanid of potassium to which has been added mercuric chlorid.
3. The process of extracting silver from its ores, which consists in subjecting the ores to the action of a solution of the cyanid of an alkaline metal to which has been added ferrocyanid of potash and mercuric chlorid.
4. The rocess of extracting silver from its ores, 'Whic consists of adding to a mill solution containing cyanid and ferrocyanid of potash, a mercuric chlorid.
5. The process of extracting silver from its ores, which consists of subjecting the ores to the action of a solution of cyanid and ferrocyanid -of potash in the presence of a chlorid of mercury and an alkali, and subsequently silver from the solution.
FRANCIS J. HOBSON.
Witnesses WM. 0. YOUNG, H. D. CLEEDE.
precipitating the
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US292555A US828288A (en) | 1905-07-18 | 1905-12-20 | Process of silver extraction. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US27030005A US827368A (en) | 1905-07-18 | 1905-07-18 | Selective solvent for silver. |
| US292555A US828288A (en) | 1905-07-18 | 1905-12-20 | Process of silver extraction. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US828288A true US828288A (en) | 1906-08-07 |
Family
ID=2896764
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US292555A Expired - Lifetime US828288A (en) | 1905-07-18 | 1905-12-20 | Process of silver extraction. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US828288A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2492078A (en) * | 1947-08-30 | 1949-12-20 | Claude A Welch | Aircraft landing gear control |
-
1905
- 1905-12-20 US US292555A patent/US828288A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2492078A (en) * | 1947-08-30 | 1949-12-20 | Claude A Welch | Aircraft landing gear control |
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