US526099A - Paul danckwardt - Google Patents
Paul danckwardt Download PDFInfo
- Publication number
- US526099A US526099A US526099DA US526099A US 526099 A US526099 A US 526099A US 526099D A US526099D A US 526099DA US 526099 A US526099 A US 526099A
- Authority
- US
- United States
- Prior art keywords
- cylinder
- silver
- gold
- paul
- tank
- 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
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- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 12
- 229910052709 silver Inorganic materials 0.000 description 12
- 239000004332 silver Substances 0.000 description 12
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 10
- 239000010931 gold Substances 0.000 description 10
- 229910052737 gold Inorganic materials 0.000 description 9
- NNFCIKHAZHQZJG-UHFFFAOYSA-N potassium cyanide Chemical compound [K+].N#[C-] NNFCIKHAZHQZJG-UHFFFAOYSA-N 0.000 description 7
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 6
- 239000003513 alkali Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 229910000497 Amalgam Inorganic materials 0.000 description 4
- 230000005611 electricity Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- UYJXRRSPUVSSMN-UHFFFAOYSA-P ammonium sulfide Chemical compound [NH4+].[NH4+].[S-2] UYJXRRSPUVSSMN-UHFFFAOYSA-P 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 229910001316 Ag alloy Inorganic materials 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 229910001020 Au alloy Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/20—Electrolytic production, recovery or refining of metals by electrolysis of solutions of noble metals
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/92—Metals of platinum group
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- PAUL DANCKVARDT OF NEW' YORK, N. Y., ASSIGNOR OF ONE-HALF TO CHARLES DOEHRING, OF SAME PLACE.
- This invention relates to an improved apparatus and process for extracting gold and silver from ores by electrolysis.
- yIt consists essentially in treating the ores in a finely pulverized state with a solution of cyanide of potassium and ammonium sullide, or another alkali sulfide, and subjecting it simultaneously to the action of an electric current and an amalgamated cathode.
- Figure l is a cross section of myimproved apparatus, on
- Fig. 2 is a longitudinal sec! tion, partly in elevation, of the same, and Fig. 3 a cross section, partly in elevation, of a supplemental apparatus.
- the letter a represents an iron cylinder provided with a lead lining b, and revolved by a belt c', and toothed wheel c, that engages a toothed wheel c2, embracing the cylin/der.
- the heads a', of the cylinder a are made of annular shape and receive Within their central opening, a second drum or cylinder cZ, composed of amalgamated sheet copper.
- This cylinder closes the openings within the heads a', and is insulated from such heads.
- the insulation is effected preferably by a rubber packing e, that embraces the inner edge of heads a', and to which a metal ring e', is connected by bolts e2. To this ring in turn the cylinder d, is secured by screws e3.
- the pulverized ore is introduced into the apparatus through door t', together with a solution of cyanide of potassium and ammonium sulfide, or another alkali sulfide.
- the proportions should be for one ton of ore,
- alkali sulfide will favor the solution of certain silver combinations, because the electric current will cause a partial oxidation of the sulfide, into hyposulite, which will thus be able to exert its dissolving power upon the silver combinations.
- each tank contains a revolublc cylinder Z, hung on shaft Z, which is insulated from tank lc, by rubber washer Z2.
- the distance between cylinder and tank should be about four centimeters, the drawings showing such distance enlarged for the sake of clearness.
- the tanks 7c are amalgamated upon their inner side and contain a little mercury besides the solution to be treated.
- Each tank la is connected with the negative pole of an electric generator by coil n, while the cylinder Z, is connected to the positive pole by coil n', and constitutes the anode.
- the filtered solution taken from the main apparatus is introduced into the uppermost tank k, by
- I employ the auxiliary apparatus generally for precipitating any cyanide solutions that contain gold and silver, and especially for precipitating solutions of gold and silver and cyanide of potassium.
- That I claim is- 1.
- the process of extracting gold and silver from ores which consists in subjecting the same simultaneously to the action ot' cyanide of potassium, an alkali sulfide and. to electrolysis, substantially as specied.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Electrolytic Production Of Metals (AREA)
Description
(No Model.)
P. DANCK-WARDT. .APPARATUS PoR AND PROCESS oP RXTRAGTING GOLD 0R SILVER PROM oRRS.
Patented Sept. 18, 1894.
m/QILZ'OPS Zag MM we Nnn PETERS co.. mom-mno.. wAsHmm-cw. n, c.
UNITED STATES PATENT OFFICE.
PAUL DANCKVARDT, OF NEW' YORK, N. Y., ASSIGNOR OF ONE-HALF TO CHARLES DOEHRING, OF SAME PLACE.
APPARATUS FOR AND PROCESS 0F EXTRACTING GOLD OR SILVER FROM ORES.
SPECIFICATION forming part of Letters Patent No. 526,099, dated September 18, 1894.
' Application filed April 2, 1894. Serial No. 505,999. (No model.)
To OZZZ whom/.it may concern:
Be it known that I, PAUL DANCKWARDT, of New York city, New York, have invented an Improved Apparatus for and Process of Extracting Gold or Silver from Ores, of which thefollowing is a specification.
This invention relates to an improved apparatus and process for extracting gold and silver from ores by electrolysis.
yIt consists essentially in treating the ores in a finely pulverized state with a solution of cyanide of potassium and ammonium sullide, or another alkali sulfide, and subjecting it simultaneously to the action of an electric current and an amalgamated cathode.
In the accompanying drawings, Figure l is a cross section of myimproved apparatus, on
line 1, 1, Fig 2. Fig. 2 is a longitudinal sec! tion, partly in elevation, of the same, and Fig. 3 a cross section, partly in elevation, of a supplemental apparatus.
The letter a, represents an iron cylinder provided with a lead lining b, and revolved by a belt c', and toothed wheel c, that engages a toothed wheel c2, embracing the cylin/der. The heads a', of the cylinder a, are made of annular shape and receive Within their central opening, a second drum or cylinder cZ, composed of amalgamated sheet copper. vThis cylinder closes the openings within the heads a', and is insulated from such heads. The insulation is effected preferably by a rubber packing e, that embraces the inner edge of heads a', and to which a metal ring e', is connected by bolts e2. To this ring in turn the cylinder d, is secured by screws e3.
To the inner periphery of cylinder a, there are secured a number of inclined radial blades f, that reach to within a short distance of cylinder CZ, and serve to shovel the ore in thin streams slowly over the surface of the inner cylinder. The electricity is conveyed to the apparatus by the contact springs g, h, connected respectively to the cylinders d, a, and of which the cylinder a, constitutes the anode, and the cylinder oZ, the cathode.
In use the pulverized ore is introduced into the apparatus through door t', together with a solution of cyanide of potassium and ammonium sulfide, or another alkali sulfide. The proportions should be for one ton of ore,
about ten pounds cyanide of potassium and two to three pounds of ammonium sulfide. The door is then closed, the drum is rotated and a constant current of electricity under low tension is turned on. This current will cause the gold and silver to be separated at the anode and to be deposited upon the amalgamated cathode. The alkali sulfide will reduce the consumption of cyanide of potassium to a minimum, because it will prevent the formation of soluble combinations between any of the raw metal combinations and part of the cyanide of potassium. Moreover the alkali sulfide will favor the solution of certain silver combinations, because the electric current will cause a partial oxidation of the sulfide, into hyposulite, which will thus be able to exert its dissolving power upon the silver combinations.
After the apparatus has rotated for several hours, all or nearly all of the gold and silver is deposited upon the inner cylinder OZ, in the form of amalgam. If this precipitation has been perfect, the apparatus is arrested, the inner cylinder is removed and the amalgam is scraped off. This amalgam is heated in a retort to obtain a gold and silver alloy, and the filtered solution goes to a storage tank to be used over again. If however the precipitation upon the inner cylinder should not have been perfect, I prefer to employ the auxiliary apparatus illustrated in Fig. 3. This apparatus is a modification of the one illustrated in Figs. 1 and 2, and consists of a series of semi-cylindrical tanks Zt, arranged one below the other.A Each tank contains a revolublc cylinder Z, hung on shaft Z, which is insulated from tank lc, by rubber washer Z2. The distance between cylinder and tank should be about four centimeters, the drawings showing such distance enlarged for the sake of clearness.
The tanks 7c, are amalgamated upon their inner side and contain a little mercury besides the solution to be treated. Each tank la, is connected with the negative pole of an electric generator by coil n, while the cylinder Z, is connected to the positive pole by coil n', and constitutes the anode. The filtered solution taken from the main apparatus is introduced into the uppermost tank k, by
IOO
pipe p. All the cylinders l, are rotated and a constant current of electricity under low tension is turned on. As soon as the uppermost tank has become filled, the solution will enter the second tank by pipe Ap', and thence through pipe p2, the third tank, to finally leave the apparatus through pipe p3, free from gold and silver. The latter is deposited in the form of amalgam upon the bottom of the tanks.
I employ the auxiliary apparatus generally for precipitating any cyanide solutions that contain gold and silver, and especially for precipitating solutions of gold and silver and cyanide of potassium.
That I claim is- 1. The process of extracting gold and silver from ores which consists in subjecting the same simultaneously to the action ot' cyanide of potassium, an alkali sulfide and. to electrolysis, substantially as specied.
2. The combination of au outer revolving drum with an inner insulated amalgamated drum, blades secured to the outer drum, and electric connections secured to the outer and inner drum, substantially as specified.
3. The combination of a series of communicating tanks with revolving insulated drums hung Within such tanks, and with electric connections secured to the tanks and drums, substantially as specified.
4. The combination of a main apparatus consisting of a revolving outer drum having blades, an insulated inner drum and electric connections, with an auxiliary apparatus consisting of a series of communicating tanks, rotating insulated drums and electric connections, substantially as specitied.
In testimony whereof I have signed this specification this 28th day of March, 1894.
PAUL DANOKWARD'I. Witnesses:
F. v. BRIESEN, WILLIAM SCHULZ.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US526099A true US526099A (en) | 1894-09-18 |
Family
ID=2594889
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US526099D Expired - Lifetime US526099A (en) | Paul danckwardt |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US526099A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2456185A (en) * | 1944-11-23 | 1948-12-14 | Gen Motors Corp | Electroplating apparatus |
| US2868709A (en) * | 1957-11-13 | 1959-01-13 | Metal & Thermit Corp | Feed device for continuous plating barrel |
-
0
- US US526099D patent/US526099A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2456185A (en) * | 1944-11-23 | 1948-12-14 | Gen Motors Corp | Electroplating apparatus |
| US2868709A (en) * | 1957-11-13 | 1959-01-13 | Metal & Thermit Corp | Feed device for continuous plating barrel |
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