US556092A - Oscar frolich - Google Patents

Oscar frolich Download PDF

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US556092A
US556092A US556092DA US556092A US 556092 A US556092 A US 556092A US 556092D A US556092D A US 556092DA US 556092 A US556092 A US 556092A
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metals
oscar
noble
tension
frolich
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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

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  • OSCAR FROLIOI-I OF BERLIN, GERMANY, ASSIGNOR TO SIEMENS dz; HALSKE, OF SAME PLACE.
  • This invention relates to the extraction of noble metals from ores, and has for its purpose to obtain those metals free from the other metals present in the ore. If the ore contains besides the noble metalssuch as gold, silver, or platina-ap onsiderable amount of other metals, the extracting process is usually carried out in the way that the latter are removed or remain in the residue, so as to obtain a solution of substantially the noble metals, as especially is the case in treating the ores with chlorine.
  • the degree of electric tension to be applied is dependent upon different circumstances-- viz.,the acids the diiferent metals are combined with, the concentration of the solution, and the nature of the different metals. It is practically sufficient to state by experiments the limits of the electric tension for the lye which is obtained from the metallurgical process, so as to operate within these limits with the result of separating the noble metals. The limits of the electric tension, however, must be determined anew when from any cause the constitution of the lye gets altered.
  • JOHN B JAoKsoN, OSCAR BIELEFELD.

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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)
  • Manufacture And Refinement Of Metals (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

UNITED STATES PATENT OFFICE.
OSCAR FROLIOI-I, OF BERLIN, GERMANY, ASSIGNOR TO SIEMENS dz; HALSKE, OF SAME PLACE.
PROCESS OF EXTRACTING NOBLE METALS FROM ORES.
SPECIFICATION forming part of Letters Patent No. 556,092, dated March 10, 1896.
Application filed August 3,1895. Serial No. 558,134.
To aZZ whom it may concern:
Be it known that I, OSCAR FROLIOH, a citizen of the Swiss Republic, residing at Berlin,
in the German Empire, have invented certain new and useful Improvements in Processes of Extracting Noble Metals from Ores; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.
This invention relates to the extraction of noble metals from ores, and has for its purpose to obtain those metals free from the other metals present in the ore. If the ore contains besides the noble metalssuch as gold, silver, or platina-ap onsiderable amount of other metals, the extracting process is usually carried out in the way that the latter are removed or remain in the residue, so as to obtain a solution of substantially the noble metals, as especially is the case in treating the ores with chlorine. The removing of the ignoble metals frequently is a difficult operation, but was considered necessary on account of the known methods not being capable of allowing the noble metals to be obtained from the final solution separately from other metals contained therein, so that a mixture would have resulted from which the noble metals were to be extracted by a separate process. It is, however, possible to extract by the aid of electrolysis the noble metals from a lye containing also other metals, it being only necessary to so control the tension of the current that the ignoble metals are allowed to remain dissolved, while the noble ones are caused to separate out with practically sufiicient speed. When a solution containing several metals is subjected to electrolysis and the tension of the current gradually increased, the metals will be caused to separate out in the order of the places they occupy in the tension seriesthat is to say, that metal which is most electronegative will be deposited first, then the next one in the series, and so on. Therefrom it results that the noble metals being of the highest electronegative order will first separate out, while the ignoble ones will not be deposited until the tension of the current has sufficiently increased. If, therefore, the electric tension is kept below that limit on which iguoble metals commence. separating out, the noble ones (N0 specimens.)
alone are deposited, and when the operation is continued for a sufficientlength of time all the amount of the latter will come out. It is obvious that by this way it is also possible to separate the noble metals from each other; but as for this purpose the electric tension would have to be altered within so narrow limits as to make it a rather troublesome operation, and as, on the other hand, it is de sired to obtain all the noble metals present, it will practically be sufficient to extract all of them in one operation.
The degree of electric tension to be applied is dependent upon different circumstances-- viz.,the acids the diiferent metals are combined with, the concentration of the solution, and the nature of the different metals. It is practically sufficient to state by experiments the limits of the electric tension for the lye which is obtained from the metallurgical process, so as to operate within these limits with the result of separating the noble metals. The limits of the electric tension, however, must be determined anew when from any cause the constitution of the lye gets altered. For instance, I mention that in operating on a lye which contains five grains each of chloride of gold, copper, and iron in one pint, and using alead cathode,a carbon anode and a current density of twelve amperes for each two square yards of cathode-surface, the limits of electric tension were between 1.2 and Let voltsviz., mere traces of copper and iron were precipitated within these limits, while gold separated completely and with sufficient speed.
What I claim is The process of extracting precious metals from a lye containing also inferior metals, said lye containing substantially five grains of each of the said metals to the pint, which consists in subjecting the said lye to the ac- 5 OSCAR FROLIOH. Witnesses:
JOHN B. JAoKsoN, OSCAR BIELEFELD.
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3926752A (en) * 1973-04-09 1975-12-16 John C Loretto Direct recovery of metals from sulphide ores by leaching and electrolysis
US3956087A (en) * 1974-05-17 1976-05-11 Mineral Research & Development Corporation Electrochemical mining of copper
US3957601A (en) * 1974-05-17 1976-05-18 Mineral Research & Development Corporation Electrochemical mining
US3959096A (en) * 1975-01-17 1976-05-25 Langer Stanley H Electrochemical recovery of copper from alloy scrap
US3959092A (en) * 1972-11-16 1976-05-25 Kabushiki Kaisha Toyota Chuo Kenkyusho Method for a surface treatment of cemented carbide article
US4026776A (en) * 1970-12-02 1977-05-31 Mitsui Mining & Smelting Co., Ltd. Method for producing high purity lead
US4071421A (en) * 1976-08-11 1978-01-31 Sherritt Gordon Mines Limited Process for the recovery of zinc
US4304646A (en) * 1980-10-27 1981-12-08 Enthone, Incorporated Method for selective removal of copper contaminants from activator solutions containing palladium and tin
US4381225A (en) * 1979-04-09 1983-04-26 Dextec Metallurgical Pty. Ltd. Production of lead from ores and concentrates
US4474654A (en) * 1982-08-27 1984-10-02 Outokumpu Oy Method for removing arsenic from a sulphuric-acid solution
US4557812A (en) * 1983-08-10 1985-12-10 National Research Development Corporation Purifying mixed-cation electrolyte
US4670116A (en) * 1985-04-03 1987-06-02 National Research Development Corporation Purifying mixed-cation electrolyte

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4026776A (en) * 1970-12-02 1977-05-31 Mitsui Mining & Smelting Co., Ltd. Method for producing high purity lead
US3959092A (en) * 1972-11-16 1976-05-25 Kabushiki Kaisha Toyota Chuo Kenkyusho Method for a surface treatment of cemented carbide article
US3926752A (en) * 1973-04-09 1975-12-16 John C Loretto Direct recovery of metals from sulphide ores by leaching and electrolysis
US3956087A (en) * 1974-05-17 1976-05-11 Mineral Research & Development Corporation Electrochemical mining of copper
US3957601A (en) * 1974-05-17 1976-05-18 Mineral Research & Development Corporation Electrochemical mining
US3959096A (en) * 1975-01-17 1976-05-25 Langer Stanley H Electrochemical recovery of copper from alloy scrap
US4071421A (en) * 1976-08-11 1978-01-31 Sherritt Gordon Mines Limited Process for the recovery of zinc
US4381225A (en) * 1979-04-09 1983-04-26 Dextec Metallurgical Pty. Ltd. Production of lead from ores and concentrates
US4304646A (en) * 1980-10-27 1981-12-08 Enthone, Incorporated Method for selective removal of copper contaminants from activator solutions containing palladium and tin
US4474654A (en) * 1982-08-27 1984-10-02 Outokumpu Oy Method for removing arsenic from a sulphuric-acid solution
US4557812A (en) * 1983-08-10 1985-12-10 National Research Development Corporation Purifying mixed-cation electrolyte
US4670116A (en) * 1985-04-03 1987-06-02 National Research Development Corporation Purifying mixed-cation electrolyte

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