US499726A - Production of alloys by electro-deposition - Google Patents
Production of alloys by electro-deposition Download PDFInfo
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- US499726A US499726A US499726DA US499726A US 499726 A US499726 A US 499726A US 499726D A US499726D A US 499726DA US 499726 A US499726 A US 499726A
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- cathode
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- 229910045601 alloy Inorganic materials 0.000 title description 33
- 239000000956 alloy Substances 0.000 title description 33
- 238000004070 electrodeposition Methods 0.000 title description 7
- 238000004519 manufacturing process Methods 0.000 title description 4
- 239000002184 metal Substances 0.000 description 36
- 229910052751 metal Inorganic materials 0.000 description 36
- 150000002739 metals Chemical class 0.000 description 24
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 11
- 239000011701 zinc Substances 0.000 description 11
- 229910052725 zinc Inorganic materials 0.000 description 11
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 10
- 239000010949 copper Substances 0.000 description 10
- 229910052802 copper Inorganic materials 0.000 description 10
- 229940108928 copper Drugs 0.000 description 10
- 238000000151 deposition Methods 0.000 description 8
- 239000003792 electrolyte Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 229910001369 Brass Inorganic materials 0.000 description 6
- 239000010951 brass Substances 0.000 description 6
- 230000005611 electricity Effects 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 230000008021 deposition Effects 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000005275 alloying Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 241001275902 Parabramis pekinensis Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 235000014987 copper Nutrition 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 239000002659 electrodeposit Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/56—Electroplating: Baths therefor from solutions of alloys
- C25D3/58—Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of copper
Definitions
- My invention relates to the art or method of producing alloys of metals by electro deposition as for example, producing brass by the deposition of copper and zinc. Alloys have been produced by fusion in the ordinary manner, by melting together two or more metals. This method has been in some instances unsatisfactory when zinc is employed because being a volatilizable and also an oxidizable metal it tends to pass into the air instead of alloying with other metals, copper for instance, in the making of the alloys called brasses. To prevent oxidation charcoal is used in the melting pot which being sometimes impure presents asource of impurity to the brass.
- the present invention consists mainly in employing separate anodes each composed of one of the metals to enter into the alloy to be deposited, and a revolving cathode which is kept continually in movement during the deposition so that each part of its surface is presented first in proximity to one of the anodes and then in proximity to the other, and in employing separate currents or currents of different density between the different anodes and the cathode so that the deposit from each anode may be regulated independently of the deposit from the other anode or anodes in order to produce the desired percentage of the different metals in the resulting deposit upon the cathode.
- Serial No. 407,681 filed October 9, 1891, I have shown and described an electrolytic apparatus in which a revolving cathode is employed. and means pro vided for using currents of different density in forming the deposit, but in that apparatus the anode although parts was of a single metal so that the resulting deposit was a single metal and not an alloy, the object of the employment of the different currents being in that case to produce a superior texture of the resulting deposit and not as in the present case, to control the composition of the said deposit.
- Figure l is a sectional view of an electrolytic apparatus adapted to be used for the production of a metal alloy by electro deposition, in accordance with this invention, and Fig. 2 a perspective view showing a modified arrangement of the anodes.
- the apparatus employed for depositing me tallic alloys in accordance with this invention may be of usual construction and is shown as comprising a vat or tank a to contain the electrolytic solution, and a revolving cathode b which may be supported and revolved in composed of separate said solution in the usual manner, the specific construction of said apparatus constituting no part of the present invention.
- On one side of the cathode are anodes K of one metal, copper for instance, and on the other side of the cylindrical cathode are anodes Z of another metal, zinc for instance, arranged Y. in the vat which contains the electrolyte.
- the electrolyte is a solution containing salts of all the metals serving as anodes, and of course varies accordingly.
- the anodes are connected with a suitable source of electricity, preferably separate currents as indicated in my former application referred to. In the latter case I find it advantageous to have separate brushes or trailers T, T to conductthe currents from the cathode.
- the cathode is made of suitable material from which the deposited alloy may be separated if desired, when formed of sufficient thickness.
- Fig. 1 the sources of electricity are indicated by the conventional representation of batteries B, B the former having one pole connected by wire 2, with the anode Z, and the other pole connected by wire 8, with the contact brush Twhile the battery B has one pole connected by wire 4:, with the anode K, and the other by wire 5, with the brush T
- each part of its surface first passes the anodes of copper, and is acted upon by a current of sufficient density to deposit the required percentage of copper, and then immediately afterward passes the anodes of zinc, through a current of sufficient density to deposit the required percentage of zinc, and I am thus enabled to produce alloys of beauty and usefulness.
- Brass and some few alloys have been electro-deposited at various times, and by myself, by using solutions of the alloy and anodes of the same alloy.
- the great difficulty in electro-deposition of brass lies in preserving the uniformity of color of the deposit.
- Each salt in the electrolyte offers a difierent resistance to the current, and hence its intensity varies or tends to vary, the composition and the color of the deposited brass.
- a feeble current chiefly decomposes the copper salt, the deposit being Very reddish; on the other hand, a current of too great an intensity decomposes the solution of zinc too rapidly and the resultingdeposit is whitish, or bluishwhite.
- the alloy may be formed and built up to any desired thickness as indicated; and by increasing or diminishing the relatively unlike densities of either of the currents, passing through the different anodes, I am enabled to increase or lessen the deposition and alloying of the corresponding metal and thus to vary at will the composition of the resulting alloy.
- WVhen four or more dilferent metals are employed as anodes, arrangement of them is carried out in a similar way and by so doing I find apparently almost no limit to the variations of this method of depositing alloys,
- the conductors 30, 50 leading from the other terminals of the said sources of electricity may be branched as shown at 81, 32, and 51, 52, said branches containing resistance R by which the current delivered through the said branches to the anodes Z and N from the course B, and to the anodes K and N from the course B may be properly controlled, and it is obvious that a single source of electricity might be employed by a similar branching of the conductors and control of the portion of the current flowing therethrough. It will be perceived that bars, sheets or slabs of alloy can be made directly according to the surface, form and preparation of the revolving cathode.
- the alloys may be so deposited as to adhere, and permanently coat the revolving cathode surface, when desirable as in the case of pipes or tubes. It appears, taking the alloying of cop per and zinc for an example, that the film deposit of copper first deposited, as the cathode revolves through the current and electrolyte at the copper anode surface, being succeeded almost instantly by the film deposit of zinc, or copper with zinc, deposited as the cathode revolves through the current and electrolyte at the zinc anode surface, is at once alloyed and thus the process of deposition, alloying, and building up goes on, to the desired thickness.
- I claim IOC 1 That improvement in the art or method of producing alloys by electro-deposition of metals, which consists in passing a current from separate anodes ot' the several metals to enter into the alloy through an electrolyte to a cathode and so moving the cathode that its surface is repeatedly and successively presented to receive the deposit from the several separate anodes, whereby the metals of the several anodes are built up and alloyed on the cathode, substantially as and for the purpose described.
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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
NoModeL) 0. R; L TCHER.
PRODUOTION 0F ALLOYS BY ELEGTRO DEPOSITION. No. 499,726. Patented June 20, 1893.
jyz.
&
THE Nonms PETERS ca, mo'rau'ruq. WASNiNGTON u c UNITED STATES PATENT OFFICE.
CHARLES R. FLETCHER, OF BOSTON, MASSACHUSETTS.
PRODUCTION OF ALLOYS. BY ELECTRO-DEPOSITION.
SPECIFICATION forming part of Letters Patent No. 499,726, dated June 20, 1893.
Application filed February 18, 1892. Serial No. 421,918- (No model.)
To all whom it may concern.-
Be itknown that I, CHARLES R. FLETCHER, of Boston, county of Suffolk, State of Massachusetts, have invented an Improvement in the Production of Alloys by Electro-Deposition, of which the following description, in connection with the accompanying drawings, is a specification, like letters and numerals on the drawings representing like parts.
My invention relates to the art or method of producing alloys of metals by electro deposition as for example, producing brass by the deposition of copper and zinc. Alloys have been produced by fusion in the ordinary manner, by melting together two or more metals. This method has been in some instances unsatisfactory when zinc is employed because being a volatilizable and also an oxidizable metal it tends to pass into the air instead of alloying with other metals, copper for instance, in the making of the alloys called brasses. To prevent oxidation charcoal is used in the melting pot which being sometimes impure presents asource of impurity to the brass. Attempts have been made to produce electro deposits of an alloyed metal usually by eniploying the required alloy as an anode and causing the same to be decomposed and deposited upon a cathode in the same manner as a single metal, and a plan has also been disclosed in which separate anode plates of the difierent metals to enter into the alloyare used, the deposits from which are made simultaneously upon a given portion of the surface of the cathode so that a deposit of all the metals entering into the alloy is produced upon any given part of the surface at any given moment. By this plan a homogeneous deposit is produced at a given point on the cathode surface but the deposit throughout the entire surface of the cathode is not homogeneous or a uniform mixture of the different metals as will be explained.
The methods of electro depositing alloys that have been heretofore practiced are deficient owing to the defect in controlling the percentages of the metals entering into the alloy, as it is by no means certain that the metals will be deposited in the same proportions as those existing in the alloy employed as an anode from which the deposit is made, and when separate anode plates of the different metals are employed it is difficult to obtain a homogeneous alloy as each anode plate must necessarily be nearer some parts of the cathode than the other since two anode plates cannot occupy the same place at the same time and it is found necessary to use great care and to frequently adjust the position of the separate anode plates in the solution as the composition of the alloy is observed to vary.
The present invention consists mainly in employing separate anodes each composed of one of the metals to enter into the alloy to be deposited, and a revolving cathode which is kept continually in movement during the deposition so that each part of its surface is presented first in proximity to one of the anodes and then in proximity to the other, and in employing separate currents or currents of different density between the different anodes and the cathode so that the deposit from each anode may be regulated independently of the deposit from the other anode or anodes in order to produce the desired percentage of the different metals in the resulting deposit upon the cathode.
In another application, Serial No. 407,681, filed October 9, 1891, I have shown and described an electrolytic apparatus in which a revolving cathode is employed. and means pro vided for using currents of different density in forming the deposit, but in that apparatus the anode although parts was of a single metal so that the resulting deposit was a single metal and not an alloy, the object of the employment of the different currents being in that case to produce a superior texture of the resulting deposit and not as in the present case, to control the composition of the said deposit.
Figure l is a sectional view of an electrolytic apparatus adapted to be used for the production of a metal alloy by electro deposition, in accordance with this invention, and Fig. 2 a perspective view showing a modified arrangement of the anodes.
The apparatus employed for depositing me tallic alloys in accordance with this invention may be of usual construction and is shown as comprising a vat or tank a to contain the electrolytic solution, and a revolving cathode b which may be supported and revolved in composed of separate said solution in the usual manner, the specific construction of said apparatus constituting no part of the present invention. On one side of the cathode, are anodes K of one metal, copper for instance, and on the other side of the cylindrical cathode are anodes Z of another metal, zinc for instance, arranged Y. in the vat which contains the electrolyte.
The electrolyte is a solution containing salts of all the metals serving as anodes, and of course varies accordingly. The anodes are connected with a suitable source of electricity, preferably separate currents as indicated in my former application referred to. In the latter case I find it advantageous to have separate brushes or trailers T, T to conductthe currents from the cathode. The cathode is made of suitable material from which the deposited alloy may be separated if desired, when formed of sufficient thickness.
In Fig. 1 the sources of electricity are indicated by the conventional representation of batteries B, B the former having one pole connected by wire 2, with the anode Z, and the other pole connected by wire 8, with the contact brush Twhile the battery B has one pole connected by wire 4:, with the anode K, and the other by wire 5, with the brush T By revolving the cathode, each part of its surface first passes the anodes of copper, and is acted upon by a current of sufficient density to deposit the required percentage of copper, and then immediately afterward passes the anodes of zinc, through a current of sufficient density to deposit the required percentage of zinc, and I am thus enabled to produce alloys of beauty and usefulness.
Brass and some few alloys have been electro-deposited at various times, and by myself, by using solutions of the alloy and anodes of the same alloy. The great difficulty in electro-deposition of brass lies in preserving the uniformity of color of the deposit. Each salt in the electrolyte offers a difierent resistance to the current, and hence its intensity varies or tends to vary, the composition and the color of the deposited brass. In practice a feeble current chiefly decomposes the copper salt, the deposit being Very reddish; on the other hand, a current of too great an intensity decomposes the solution of zinc too rapidly and the resultingdeposit is whitish, or bluishwhite. But by my invention, the alloy may be formed and built up to any desired thickness as indicated; and by increasing or diminishing the relatively unlike densities of either of the currents, passing through the different anodes, I am enabled to increase or lessen the deposition and alloying of the corresponding metal and thus to vary at will the composition of the resulting alloy.
In cases Where I wish to deposit three metals, to form an alloy, I prefer to arrange (as shown in Fig. 2) alternate anodesN of one of the three metals on each side of the revolving cathode, and between the anodes K of the second metal on one side, and between the anodes Z of the third metal on the otherside of the revolving cathode. And I adapt the length and width of the several anodes of several metals to my desires concerning the resulting alloy and to the solution of these several metals which form the electrolyte.
WVhen four or more dilferent metals are employed as anodes, arrangement of them is carried out in a similar way and by so doing I find apparently almost no limit to the variations of this method of depositing alloys,
I prefer to use separate sources of electricity as indicated at B, B Figs. 1 and 2 (the currents of dynamo electric machines being generally preferable) the said sources of electricity each having one terminal connected by wires 2 and 4, respectively with contact brushes T, T engaging the cathode, and when more than two metals are employed as anodes as shown in Fig. 2, the conductors 30, 50 leading from the other terminals of the said sources of electricity may be branched as shown at 81, 32, and 51, 52, said branches containing resistance R by which the current delivered through the said branches to the anodes Z and N from the course B, and to the anodes K and N from the course B may be properly controlled, and it is obvious that a single source of electricity might be employed by a similar branching of the conductors and control of the portion of the current flowing therethrough. It will be perceived that bars, sheets or slabs of alloy can be made directly according to the surface, form and preparation of the revolving cathode. The alloys may be so deposited as to adhere, and permanently coat the revolving cathode surface, when desirable as in the case of pipes or tubes. It appears, taking the alloying of cop per and zinc for an example, that the film deposit of copper first deposited, as the cathode revolves through the current and electrolyte at the copper anode surface, being succeeded almost instantly by the film deposit of zinc, or copper with zinc, deposited as the cathode revolves through the current and electrolyte at the zinc anode surface, is at once alloyed and thus the process of deposition, alloying, and building up goes on, to the desired thickness.
I am aware that brass has been formed by a thick deposit of zinc upon a thick deposit of copper over a stationary iron or steel object, and then submitting to heat until the metals become alloyed with eachother; then repeating these three steps if desirable, but this is quite different from my invention and method, in which the different metals entering into the alloy are deposited successively so to speak, but each succeeds the other so immediately that the two practically constitute a homogeneous and uniform alloy, the relative percentage of any metal being varied by a correspondingcontrol of the current affecting it, without changing the action upon the other metal or metals.
I claim IOC 1. That improvement in the art or method of producing alloys by electro-deposition of metals, which consists in passing a current from separate anodes ot' the several metals to enter into the alloy through an electrolyte to a cathode and so moving the cathode that its surface is repeatedly and successively presented to receive the deposit from the several separate anodes, whereby the metals of the several anodes are built up and alloyed on the cathode, substantially as and for the purpose described.
2. The combination of an electrolytic vat
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US499726A true US499726A (en) | 1893-06-20 |
Family
ID=2568560
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US499726D Expired - Lifetime US499726A (en) | Production of alloys by electro-deposition |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US499726A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2903405A (en) * | 1956-05-24 | 1959-09-08 | Sabins Dohrmann Inc | Corrosion prevention system |
| US3350287A (en) * | 1962-09-06 | 1967-10-31 | M & T Chemicals Inc | Method of preventing etch on cast iron in plating baths |
-
0
- US US499726D patent/US499726A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2903405A (en) * | 1956-05-24 | 1959-09-08 | Sabins Dohrmann Inc | Corrosion prevention system |
| US3350287A (en) * | 1962-09-06 | 1967-10-31 | M & T Chemicals Inc | Method of preventing etch on cast iron in plating baths |
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