US526099A - Paul danckwardt - Google Patents

Paul danckwardt Download PDF

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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
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cylinder
silver
gold
paul
tank
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/20Electrolytic production, recovery or refining of metals by electrolysis of solutions of noble metals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • 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.
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Cited By (2)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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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