US521991A - Metallic powder - Google Patents
Metallic powder Download PDFInfo
- Publication number
- US521991A US521991A US521991DA US521991A US 521991 A US521991 A US 521991A US 521991D A US521991D A US 521991DA US 521991 A US521991 A US 521991A
- Authority
- US
- United States
- Prior art keywords
- particles
- cathode
- metallic
- instance
- metallic powder
- 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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- 239000000843 powder Substances 0.000 title description 24
- 239000002245 particle Substances 0.000 description 26
- 238000000034 method Methods 0.000 description 20
- 238000004519 manufacturing process Methods 0.000 description 12
- 239000002184 metal Substances 0.000 description 12
- 229910052751 metal Inorganic materials 0.000 description 12
- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 10
- 229910052725 zinc Inorganic materials 0.000 description 10
- 239000011701 zinc Substances 0.000 description 10
- 229910001369 Brass Inorganic materials 0.000 description 8
- 239000010951 brass Substances 0.000 description 8
- 239000004020 conductor Substances 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 150000002739 metals Chemical class 0.000 description 8
- 238000005868 electrolysis reaction Methods 0.000 description 6
- 229910045601 alloy Inorganic materials 0.000 description 4
- 239000000956 alloy Substances 0.000 description 4
- XFXPMWWXUTWYJX-UHFFFAOYSA-N cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 4
- -1 for instance Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000011780 sodium chloride Substances 0.000 description 4
- 150000003751 zinc Chemical class 0.000 description 4
- 229910000906 Bronze Inorganic materials 0.000 description 2
- 210000003414 Extremities Anatomy 0.000 description 2
- 101700047253 FLII Proteins 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000010974 bronze Substances 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 229910052570 clay Inorganic materials 0.000 description 2
- 230000001419 dependent Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000011133 lead Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 230000036633 rest Effects 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/16—Apparatus for electrolytic coating of small objects in bulk
- C25D17/28—Apparatus for electrolytic coating of small objects in bulk with means for moving the objects individually through the apparatus during treatment
Definitions
- ATTORNEY n1 mmomu. UTHOGMPNINQ counwz.
- Our invention relates to the process of manufacturing metallic powders and its novelty consists in the several successive steps of the process by which the desired result is obtained.
- the object of our invention is to produce a powder, each grain of which shall be capable of use in relations where pure bronze or other metallic powders may be employed and which shall at the same time be cheaper.
- Our discovery consists in brief, of the fact that by interposing between certain well known electrodes, during the process of electrolysis, a metallic conductor in a finely divided state and which is kept in constant agitation so that its particles are forced upon the cathode and kept'from contact with the anode these particles become covered with a shell composed of the metallic base of a salt fed between the electrodes.
- the amount of the deposit and its precise nature are dependent upon the nature of the electrodes and of the bath employed, the strength of the current, the rapidity of motion of the metallic conductor and the time of its exposure.
- Fig. 2 is a transverse section thereof on the plane of the line w,a: in Fig. 1.
- V is a box or receptacle semi 110.499.927. on specimens.
- the cathode 0 made for instance of a sheet,,of..bg a'ss in the form of a flat plate, is securedin the box in an inclined position from the inlet to the outlet aperture and rests upon a solid base b of any suitable material, for instance, cement.
- the anodeA made of a suitable material is also secured'withifthe box V mosition, for instance, substantially parallel with thatof the cathode O and it is separated from the anode by a dialytic partition D for instance, a plate of baked clay. It is necessary that the anode should be perforated or made otherwise permeable.
- Electric wires w, w are connected with the anode and cathode in the usual manner and supply a current from a source of electricity not shown.
- the brushes should be so arranged that their extremities just touch the upper surface of the cathode.
- the action of the apparatus is. as follows: Surrounding the anode is a bath B consisting of a cyanide solution, containing copper and zinc salts. There is then caused to be fed at the inlet aperture f, by any suitable means, a cyanide solution of copper and zinc salts in which is powdered zinc G, or other similar metallic conductor in a finely divided state,
- the brushes I I I are then set in rapid motion. , The particles of powdered zinc are caught by the bristles and forced over the cathode. They are thus prevented from adhering to the cathode or to each other..
- such product may be treated as follows: Itmay be 3 treated electrically or by simple immersion and its particles receive a direct deposit of other metals or alloys, for instance, nickel, silver, gold, iron, copper, brass, lead, 850., and: various shades of colorand diiferent metallic lusters may be produced by treating the met als soideposited in ways well known in the art, for instance, by using solutions composed of salts of different metals, by changing the anodes, or by treating the coated particles with different or varying degreesof heat.
- Itmay be 3 treated electrically or by simple immersion and its particles receive a direct deposit of other metals or alloys for instance, nickel, silver, gold, iron, copper, brass, lead, 850.
- various shades of colorand diiferent metallic lusters may be produced by treating the met als soideposited in ways well known in the art, for instance, by using solutions composed of salts of different metals, by changing the anodes, or by treating the coated particles with different or varying degreesof heat.
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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)
- Electrolytic Production Of Metals (AREA)
Description
(No Model.)
v J. SACHS 81; E. HUBER. PROCESS OF MANUFACTURING METALLIC POWDER.-
N0. 521,991. Pat ented June 26, 1894.
JVE/VTORS W 2% Mm f !IIIIIIIIIII/flII/IIIIIIIIIII/lflYIIIIIIIIIIM/l WITNESSES:
ATTORNEY n1: mmomu. UTHOGMPNINQ counwz.
UNITED STATES JOSEPH SACHS AND ERNEST.
PATENT OFFICE.
HUBER, on NEW YORK, N. Y.
PROCESS-OF MANUFACTURING METALLIC POWDERS.
SPECIFICATION forming part of Letters Patent No. 521,991, dated June 26,1894.
Application filed February 12, 1894.
To a whom it may concern.-
Be it known that we, JOSEPH SACHS, a subject of the Grand Duke of Baden, and ERNEST HUBER, a citizen of Switzerland, both residing in the city and county of New York and State of New York, have invented certain new and useful Improvements in Processes of Manufacturing Metallic Powders; and we do hereby declare the following to be afull, 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.
Our invention relates to the process of manufacturing metallic powders and its novelty consists in the several successive steps of the process by which the desired result is obtained.
The object of our invention is to produce a powder, each grain of which shall be capable of use in relations where pure bronze or other metallic powders may be employed and which shall at the same time be cheaper. In the course of our experiments, we have discovered a process which seems to attain this object and which we believe to be new and highly useful. Our discovery consists in brief, of the fact that by interposing between certain well known electrodes, during the process of electrolysis, a metallic conductor in a finely divided state and which is kept in constant agitation so that its particles are forced upon the cathode and kept'from contact with the anode these particles become covered with a shell composed of the metallic base of a salt fed between the electrodes. The amount of the deposit and its precise nature are dependent upon the nature of the electrodes and of the bath employed, the strength of the current, the rapidity of motion of the metallic conductor and the time of its exposure.
The mechanical apparatus which in the light of our present knowledge we think best adapted to carry out our invention we will now describe.
In the drawings, Figure 1 is a vertical central longitudinal section and partial plan view of one form of the apparatus used by us, and
Fig. 2 is a transverse section thereof on the plane of the line w,a: in Fig. 1.
In the drawings,V is a box or receptacle semi 110.499.927. on specimens.)
made of any suitable material and provided with an inlet aperture f and an outlet aperture g. The cathode 0 made for instance of a sheet,,of..bg a'ss in the form of a flat plate, is securedin the box in an inclined position from the inlet to the outlet aperture and rests upon a solid base b of any suitable material, for instance, cement. The anodeA made of a suitable material is also secured'withifthe box V mosition, for instance, substantially parallel with thatof the cathode O and it is separated from the anode by a dialytic partition D for instance, a plate of baked clay. It is necessary that the anode should be perforated or made otherwise permeable. Electric wires w, w are connected with the anode and cathode in the usual manner and supply a current from a source of electricity not shown. Mounted on shafts E journaled inthe side of the boxV in any suitable manner, and located between the anode and cathode, is a series of brushes I I I", 850., adapted to revolve, across the surface of the oathode and actuated by any suitable means quite within the range of an ordinary me chanical skill to provide, for instance, a belt and pulley. The brushes should be so arranged that their extremities just touch the upper surface of the cathode.
The action of the apparatus is. as follows: Surrounding the anode is a bath B consisting of a cyanide solution, containing copper and zinc salts. There is then caused to be fed at the inlet aperture f, by any suitable means, a cyanide solution of copper and zinc salts in which is powdered zinc G, or other similar metallic conductor in a finely divided state,
.and which-has been previously'well cleansed.
The brushes I I I", &c., are then set in rapid motion. ,The particles of powdered zinc are caught by the bristles and forced over the cathode. They are thus prevented from adhering to the cathode or to each other.. It
will be found that in a short time each particle of the powdered zinc has been completely covered mm of brass deposited thereon. The covered particles gradually drop downward by the action of gravity and the freedom of motion caused by the agitation of the solution by the brushes, until they reach the outlet aperture and are received in a suitable vessel, as H. The length of the cathode and strength of the current should be so arranged that each particle of the zinc will be completely covered by the time this outlet aperture is reached. This data should in each case be predetermined by experiment.
The product obtained by means of theprocess described when removed from the bath and dried is, so far as its external appearance goes, pure brass, and, if a powder of this kind is desired, it is ready for use after polishing.
If, however, other shadesof color are desired or surfaces of other metal are to be used, such product may be treated as follows: Itmay be 3 treated electrically or by simple immersion and its particles receive a direct deposit of other metals or alloys, for instance, nickel, silver, gold, iron, copper, brass, lead, 850., and: various shades of colorand diiferent metallic lusters may be produced by treating the met als soideposited in ways well known in the art, for instance, by using solutions composed of salts of different metals, by changing the anodes, or by treating the coated particles with different or varying degreesof heat. In
short this product may be treated as though. i
its particles were pure brass. During any such. subsequent processes, however, the grains must be kept from adhering to each other by continual agitation.
Other metallic bases for the powders, may be employed, instead of zinc,for instance, iron, copper or other alloys or metals may be deposited thereon, but the principle upon which the formation of the product depends willbe the same in each instance.
By the word powders we do not mean to confine ourselves to a material composed of particles in an impalpable form. We include within the term what are technically known as Hitters and metallics, the former consisting of flaky particles and the latter of particles larger than those to which the term powder is commonly applied and usually having well defined edges and surfaces. u Having described our invention, what we claim as new is- 1 The process of manufacturing metallic powders which consists in interposing between suitable electrodes during. the process of electrolysis ametallic conductorima finely 3 divided state maintained in motion during said process.
: a 2. Theprocess of manufacturing metallic lpowders which consists in depositing. a shell of metal by electrolysis upon each: particle of a metallic conductor while the latter isin a:
finely divided state and under conditions of constant agitation.
In testimony whereof we have signed. the specification in the presence of twosubscribing witnesses. Josnrrr sAons.
ERNEST HUBER.
Witnesses:
WM. EAIMOND BAIRD,
MAY G. RIDLEY.
Publications (1)
Publication Number | Publication Date |
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US521991A true US521991A (en) | 1894-06-26 |
Family
ID=2590788
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US521991D Expired - Lifetime US521991A (en) | Metallic powder |
Country Status (1)
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US (1) | US521991A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2421209A (en) * | 1942-01-30 | 1947-05-27 | American Smelting Refining | Electrolytic refining of metals |
US3663298A (en) * | 1970-03-03 | 1972-05-16 | North American Rockwell | Rotatable electrode structure with conductive particle bed |
US3779873A (en) * | 1971-06-01 | 1973-12-18 | De Beers Ind Diamond | Process for metal coating diamonds |
USRE28379E (en) * | 1966-05-24 | 1975-03-25 | Electrochemical process of coating using a fluidized bed | |
US3994785A (en) * | 1975-01-09 | 1976-11-30 | Rippere Ralph E | Electrolytic methods for production of high density copper powder |
US4046643A (en) * | 1975-09-09 | 1977-09-06 | Rippere Ralph E | Production of multi-metal particles for powder metallurgy alloys |
US4064033A (en) * | 1974-04-12 | 1977-12-20 | Compagnie Royale Asturienne Des Mines | Electrolytic cell for electrolytically preparing a metal in pulverulent form |
US4090927A (en) * | 1976-02-12 | 1978-05-23 | Battelle Memorial Institute | Process for electro-depositing a metal on conducting granules |
US4115210A (en) * | 1974-04-12 | 1978-09-19 | Compagnie Royale Asturienne Des Mines | Method of electrolytically preparing a metal in pulverulent form |
US4120758A (en) * | 1975-09-09 | 1978-10-17 | Rippere Ralph E | Production of powder metallurgy alloys |
-
0
- US US521991D patent/US521991A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2421209A (en) * | 1942-01-30 | 1947-05-27 | American Smelting Refining | Electrolytic refining of metals |
USRE28379E (en) * | 1966-05-24 | 1975-03-25 | Electrochemical process of coating using a fluidized bed | |
US3663298A (en) * | 1970-03-03 | 1972-05-16 | North American Rockwell | Rotatable electrode structure with conductive particle bed |
US3779873A (en) * | 1971-06-01 | 1973-12-18 | De Beers Ind Diamond | Process for metal coating diamonds |
US4064033A (en) * | 1974-04-12 | 1977-12-20 | Compagnie Royale Asturienne Des Mines | Electrolytic cell for electrolytically preparing a metal in pulverulent form |
US4115210A (en) * | 1974-04-12 | 1978-09-19 | Compagnie Royale Asturienne Des Mines | Method of electrolytically preparing a metal in pulverulent form |
US3994785A (en) * | 1975-01-09 | 1976-11-30 | Rippere Ralph E | Electrolytic methods for production of high density copper powder |
US4046643A (en) * | 1975-09-09 | 1977-09-06 | Rippere Ralph E | Production of multi-metal particles for powder metallurgy alloys |
US4120758A (en) * | 1975-09-09 | 1978-10-17 | Rippere Ralph E | Production of powder metallurgy alloys |
US4090927A (en) * | 1976-02-12 | 1978-05-23 | Battelle Memorial Institute | Process for electro-depositing a metal on conducting granules |
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