US2421863A - Process for driving out occlusions of gases like hydrogen from the surface layers of workpieces - Google Patents
Process for driving out occlusions of gases like hydrogen from the surface layers of workpieces Download PDFInfo
- Publication number
- US2421863A US2421863A US390374A US39037441A US2421863A US 2421863 A US2421863 A US 2421863A US 390374 A US390374 A US 390374A US 39037441 A US39037441 A US 39037441A US 2421863 A US2421863 A US 2421863A
- Authority
- US
- United States
- Prior art keywords
- metal
- current
- hydrogen
- gases
- occlusions
- 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
Links
- 238000000034 method Methods 0.000 title description 19
- 239000007789 gas Substances 0.000 title description 11
- 239000001257 hydrogen Substances 0.000 title description 7
- 229910052739 hydrogen Inorganic materials 0.000 title description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title description 6
- 239000002344 surface layer Substances 0.000 title description 6
- 229910052751 metal Inorganic materials 0.000 description 24
- 239000002184 metal Substances 0.000 description 24
- 239000010410 layer Substances 0.000 description 10
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 8
- 238000009713 electroplating Methods 0.000 description 8
- 238000005260 corrosion Methods 0.000 description 7
- 230000007797 corrosion Effects 0.000 description 7
- 238000011282 treatment Methods 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 4
- 150000001247 metal acetylides Chemical class 0.000 description 4
- 229910052759 nickel Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002045 lasting effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 101100001677 Emericella variicolor andL gene Proteins 0.000 description 1
- 229910052728 basic metal Inorganic materials 0.000 description 1
- 150000003818 basic metals Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000010405 reoxidation reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F1/00—Electrolytic cleaning, degreasing, pickling or descaling
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/34—Pretreatment of metallic surfaces to be electroplated
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S205/00—Electrolysis: processes, compositions used therein, and methods of preparing the compositions
- Y10S205/917—Treatment of workpiece between coating steps
Definitions
- This invention relates to a process for driving out occlusions of gases like hydrogen from the surface layers of work-pieces in an electrolytic manner to increase the resistance to corrosion of such layers.
- the most important field of application of the process is the pretreatment of metals to be coated for subsequent electroplating so as to impart to the work a surface quality adapted for placing thereon metallic deposits of any kind and producing durable coatings of high corrosion resistance.
- Electrolytic refining orcleaning processes in which the metal objects to be treated are used either as cathode or as anode in an electrolytic bath are in particular widely employed.
- anodic treatment is especially effective and, above all, applicable Where it is necessary to neutralize, as for subsequent electroplating, the hydrogen found in the surface layers of a work, which enters the metal, or is not oxidized, during cathodic cleaning as well as for instance during pickling in an acid solution.
- the invention avoids the drawbacks of the hitherto known anodic treating methods and provides a process which insures complete liberation of the surface of a. work not only from all oxide films but also from the carbides, etc., embedded in the body of the metal, as well as full oxidation of the hydrogen contained in the pores of the metal.
- the invention is based on the knowledge that the process of the dissolution of the metal and of the reoxidation thereof does not occur immediately after.
- current is applied to the bath containing the workserving as anode, but sets in, depending on the nature of the alkaline or neutral, though not acid, bath, that is an aqueous bath whose DH is at least 7, awcertain time after the current has begun to act.
- the gas reactions on the other hand, i. e. the oxidation of the hydrogen and the conversion of the carbides, etc., whose presence directly at the surface of a work subsequently to be coated is highly detrimental and absolutely prevents for instance the production of deposits free from pores in electroplating commence as soon as the current begins to act.
- the invention proposes to operate the bath in which the work, previously preferably cathodically treated to effect decreasin and removalof the surface oxide films, is used as anode by currentimpulses occurring at intervals the duration of which and of the impulses is adapted to thepeculiar nature of the metal and of the electrolyte in such manner thatthe reactions leading to the formation of an oxidic deposit of the metal on the work do not set in as yet.
- each current action diifers therefore and, depending on circumstances, may last up to seconds, though it is much shorter as a rule and may amount to less than one second.
- the actions of the current are continued until it is apparent that all oxidizable constituents, besides the metal treated, are completely oxidized at the surface. This can be well observed with the naked eye. For example, during the first current impulses islandsand band-like regions appear on a test piece, which are irregularly distributed over the entire surface and on which a particularly strong gas development can be noticed. After a certain number of impulses these at first clearly contrasting regions disappear, and the gas development proceeds uniformly over the entire area. At this moment no oxidizable constituents are present any more.
- the new process is preferably carried out with the aid of a switch connected in the circuit for automatically cutting off and interrupting the current for adjustable periods.
- electroplating 3 produces a metal layer of highest quality, which is not only completely free from pores and pitting, but which is distinguished also by an extraordinary adhesiveness to the basic metal.
- the layer produced is, moreover, much more non-corrodible than a layer obtained in the usual manner.
- the sheets were subjected to the usual corrosion test by boiling in distilled water, that is, they were boiled for four minutes and then allowed to stand four hours in their boiling water. The subsequent count of rusty places yielded 1,486 points.
- a second series of 20 sheets was treated in the same manner with the difference, however, that during the anodic treatment the current was applied only for one second whereupon the current supply was interrupted for another second.
- the sheets remained in the anodic bath for 30 seconds, but only current impulses lasting one second each were applied, so that the total current action amounted to 15 seconds.
- the application and effect of the new process have been described above with a View to employin it as a pretreating process for subsequent electroplating.
- the range of uses of the new process is. however, not limited hereto, but is far more general.
- the new process can be advantageously applied in all cases where occlusions of gas, particularly hydrogen, have to be driven out of the surface layers of work-pieces. It may serve for instance for after-treating already produced metal coatings to considerably increase their resistance to corrosion, or for giving intermediate treatment when electroplating several superposed metal layers of the same or different kind, as for instance for dehydrating a nickel layer prior to final chrome-plating.
- a process for cleaning comprising driving out of occluded gases and removal of oxide films and surface embedded impurities including carbides from the exterior layers of metals consisting in using the metal to be cleaned as an anode in an aqueous bath where the pH is at least '7, operating this bath with current impulses whose duration varies from one second to sixty seconds according to the metal to be cleaned and is sufficiently long to oxidize impurities in and on the metal surface and to remove occluded gases but is stopped before oxidation and solution of any metal of the surface takes place, repeating these anodic impulses a sufiicient number of times to bring about a gas development which is uniform over the entire surface area and depositing an additional metal layer by electro-plating.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating Methods And Accessories (AREA)
Description
Patented June 10, 1947 FFICE PROCESS FOR DRIVING OUTgOCCLUSIONS OF GASES LIKE HYDROGEN FROM THE SURFACE LAYERS OF WORKPIECES Richard Beck, Wiesbaden, Germany; vested in the Attorney General of the United States No Drawing. Application April 25,1941, Serial No. 390,374. In GermanyApril 26, 1940 3 Claims 1 This invention relates to a process for driving out occlusions of gases like hydrogen from the surface layers of work-pieces in an electrolytic manner to increase the resistance to corrosion of such layers. The most important field of application of the process is the pretreatment of metals to be coated for subsequent electroplating so as to impart to the work a surface quality adapted for placing thereon metallic deposits of any kind and producing durable coatings of high corrosion resistance.
Owing to its great advantages compared with those obtainable by the application of the formerly usually employed mechanical or chemical cleaning treatments, the electrochemical treatment of metallic Work-pieces for the purpose of removing foreign external impurities, the oxidic surface films andL foreign matter embedded in the surface layers in the course of production, particularly for preparing the surface for the subsequent provision of a deposit, has been more and more adopted of late.
Electrolytic refining orcleaning processes in which the metal objects to be treated are used either as cathode or as anode in an electrolytic bath are in particular widely employed.
Of these processes the anodic treatment is especially effective and, above all, applicable Where it is necessary to neutralize, as for subsequent electroplating, the hydrogen found in the surface layers of a work, which enters the metal, or is not oxidized, during cathodic cleaning as well as for instance during pickling in an acid solution.
The known processes of the latter class are, however, open to the objection that their application involves partial dissolution of the metal treated and redeposition of the dissolved metal in oxidic form on the surface of the work, which implicates an undesirable loss of material and necessitates also subsequent treatment of the work in a mechanical or chemical manner to remove again these oxides. The known process failed, moreover, even if the current was allowed to act for a long time, to remove with suiiicient pene trative effect the foreign constituents of the metal, especially carbides, etc., embedded between the crystallites of the metal structure, though this foreign matter is also a cause for the maniiestation of corrosion in the metal coating.
The invention avoids the drawbacks of the hitherto known anodic treating methods and provides a process which insures complete liberation of the surface of a. work not only from all oxide films but also from the carbides, etc., embedded in the body of the metal, as well as full oxidation of the hydrogen contained in the pores of the metal.
The invention is based on the knowledge that the process of the dissolution of the metal and of the reoxidation thereof does not occur immediately after. current is applied to the bath containing the workserving as anode, but sets in, depending on the nature of the alkaline or neutral, though not acid, bath, that is an aqueous bath whose DH is at least 7, awcertain time after the current has begun to act. The gas reactions, on the other hand, i. e. the oxidation of the hydrogen and the conversion of the carbides, etc., whose presence directly at the surface of a work subsequently to be coated is highly detrimental and absolutely prevents for instance the production of deposits free from pores in electroplating commence as soon as the current begins to act.
In view of these facts the invention proposes to operate the bath in which the work, previously preferably cathodically treated to effect decreasin and removalof the surface oxide films, is used as anode by currentimpulses occurring at intervals the duration of which and of the impulses is adapted to thepeculiar nature of the metal and of the electrolyte in such manner thatthe reactions leading to the formation of an oxidic deposit of the metal on the work do not set in as yet.
The duration of each current action diifers therefore and, depending on circumstances, may last up to seconds, though it is much shorter as a rule and may amount to less than one second. The actions of the current are continued until it is apparent that all oxidizable constituents, besides the metal treated, are completely oxidized at the surface. This can be well observed with the naked eye. For example, during the first current impulses islandsand band-like regions appear on a test piece, which are irregularly distributed over the entire surface and on which a particularly strong gas development can be noticed. After a certain number of impulses these at first clearly contrasting regions disappear, and the gas development proceeds uniformly over the entire area. At this moment no oxidizable constituents are present any more.
The new process is preferably carried out with the aid of a switch connected in the circuit for automatically cutting off and interrupting the current for adjustable periods.
When the above-mentioned condition has been reached, the current is shut off, the work taken out and rinsed and may then for instance be directly electroplated.
Experiments have shown that electroplating 3 produces a metal layer of highest quality, which is not only completely free from pores and pitting, but Which is distinguished also by an extraordinary adhesiveness to the basic metal.
The layer produced is, moreover, much more non-corrodible than a layer obtained in the usual manner.
At a comparison test 20 sheets were cathodically decreased in the customary way and then 'anodically treated uninterruptedly for 30 sec- After this time the test sheet did not.
onds. show any visible coat. The current wasthen cut off, and the sheets were rinsed and nickelplated for 30 minutes. a
The sheets were subjected to the usual corrosion test by boiling in distilled water, that is, they were boiled for four minutes and then allowed to stand four hours in their boiling water. The subsequent count of rusty places yielded 1,486 points.
A second series of 20 sheets was treated in the same manner with the difference, however, that during the anodic treatment the current was applied only for one second whereupon the current supply was interrupted for another second. The sheets remained in the anodic bath for 30 seconds, but only current impulses lasting one second each were applied, so that the total current action amounted to 15 seconds.
The corrosion test of these sheets, which were also immediately nickelplated for 30 minutes, disclosed only 176 rusty places, or only one-ninth of the number of such places found during the first test.
The application and effect of the new process have been described above with a View to employin it as a pretreating process for subsequent electroplating. The range of uses of the new process is. however, not limited hereto, but is far more general. The new process can be advantageously applied in all cases where occlusions of gas, particularly hydrogen, have to be driven out of the surface layers of work-pieces. It may serve for instance for after-treating already produced metal coatings to considerably increase their resistance to corrosion, or for giving intermediate treatment when electroplating several superposed metal layers of the same or different kind, as for instance for dehydrating a nickel layer prior to final chrome-plating.
At any rate, the invention is not restricted to the embodiments and possibilities of application described, but may be varied in many ways without deviating from its fundamental idea.
What is claimed is:
1. A process for cleaning, comprising driving out of occluded gases and removal of oxide films and surface embedded impurities including carbides from the exterior layers of metals consisting in using the metal to be cleaned as an anode in an aqueous bath where the pH is at least '7, operating this bath with current impulses whose duration varies from one second to sixty seconds according to the metal to be cleaned and is sufficiently long to oxidize impurities in and on the metal surface and to remove occluded gases but is stopped before oxidation and solution of any metal of the surface takes place, repeating these anodic impulses a sufiicient number of times to bring about a gas development which is uniform over the entire surface area and depositing an additional metal layer by electro-plating.
2. The process for cleaning and improving the resistance to corrosion of nickel which consists in using the metal to be cleaned as an anode in an aqueous bath whose pH is at least '7, applying a current impulse for one second, interrupting the current {or another second, repeating this application and interruption of current for thirty seconds while the nickel remains in the bath, thereby applying the current fifteen times, each application lasting only one second, producing a uniform development of gas over the entire surface area and depositin a chrome layer upon the nickel by electro-plating.
3. Process according to claim 1 in which the additional layer is subjected to treatment by intermittent anodic current impulses.
RICHARD BECK.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 2,109,675 Miller Mar. 1, 1938 1,574,055 Pedersen Feb. 23, 1926 2,133,255 Rogers Oct. 11, 1928 FOREIGN PATENTS Number Country Date 458,940 Great Britain Dec. 30, 1936
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEB190570D DE715515C (en) | 1940-04-27 | 1940-04-27 | Process for anodic pretreatment previously degreased metal surfaces in the usual way |
| DE270640X | 1940-06-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2421863A true US2421863A (en) | 1947-06-10 |
Family
ID=25763644
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US390374A Expired - Lifetime US2421863A (en) | 1940-04-27 | 1941-04-25 | Process for driving out occlusions of gases like hydrogen from the surface layers of workpieces |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US2421863A (en) |
| CH (1) | CH223783A (en) |
| DE (1) | DE715515C (en) |
| FR (1) | FR869641A (en) |
| NL (1) | NL58143C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2732288A (en) * | 1951-06-19 | 1956-01-24 | Manufacture of metal mesh screens | |
| DE939659C (en) * | 1952-06-28 | 1956-03-01 | Richard Dr Springer | Process for the electrolytic descaling of metal surfaces in alkaline solutions |
| US2850444A (en) * | 1954-11-01 | 1958-09-02 | Rca Corp | Pulse method of etching semiconductor junction devices |
| US3331760A (en) * | 1962-01-16 | 1967-07-18 | Gen Dynamics Corp | Electrolytic milling |
| US3886053A (en) * | 1973-11-01 | 1975-05-27 | James M Leland | Programmable pulse electroplating process |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1079417B (en) * | 1955-06-25 | 1960-04-07 | Siemens Ag | Process for the electrolytic surface treatment of metals |
| DE1228493B (en) * | 1960-11-23 | 1966-11-10 | Schoeller & Co | Process for cleaning metal objects by ultrasonic treatment |
| US3671407A (en) * | 1970-09-11 | 1972-06-20 | United States Steel Corp | Method for preventing high-temperature blistering of copper coatings electro-deposited on copper substrates |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1574055A (en) * | 1920-05-15 | 1926-02-23 | Madsenell Corp | Fabrication of metal sheets by electrodeposition |
| GB458940A (en) * | 1935-08-20 | 1936-12-30 | Richard Thomas & Co Ltd | Improvements in or relating to the production of coatings of tin or tin alloys on metal articles |
| US2109675A (en) * | 1934-10-03 | 1938-03-01 | Meaker Company | Method of eliminating embrittlement and corrosion of pickled metal |
| US2133255A (en) * | 1937-05-19 | 1938-10-11 | Percy A E Armstrong | Process of electroplating copper |
-
1940
- 1940-04-27 DE DEB190570D patent/DE715515C/en not_active Expired
- 1940-10-22 NL NL99295A patent/NL58143C/xx active
- 1940-11-28 CH CH223783D patent/CH223783A/en unknown
-
1941
- 1941-01-30 FR FR869641D patent/FR869641A/en not_active Expired
- 1941-04-25 US US390374A patent/US2421863A/en not_active Expired - Lifetime
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1574055A (en) * | 1920-05-15 | 1926-02-23 | Madsenell Corp | Fabrication of metal sheets by electrodeposition |
| US2109675A (en) * | 1934-10-03 | 1938-03-01 | Meaker Company | Method of eliminating embrittlement and corrosion of pickled metal |
| GB458940A (en) * | 1935-08-20 | 1936-12-30 | Richard Thomas & Co Ltd | Improvements in or relating to the production of coatings of tin or tin alloys on metal articles |
| US2133255A (en) * | 1937-05-19 | 1938-10-11 | Percy A E Armstrong | Process of electroplating copper |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2732288A (en) * | 1951-06-19 | 1956-01-24 | Manufacture of metal mesh screens | |
| DE939659C (en) * | 1952-06-28 | 1956-03-01 | Richard Dr Springer | Process for the electrolytic descaling of metal surfaces in alkaline solutions |
| US2850444A (en) * | 1954-11-01 | 1958-09-02 | Rca Corp | Pulse method of etching semiconductor junction devices |
| US3331760A (en) * | 1962-01-16 | 1967-07-18 | Gen Dynamics Corp | Electrolytic milling |
| US3886053A (en) * | 1973-11-01 | 1975-05-27 | James M Leland | Programmable pulse electroplating process |
Also Published As
| Publication number | Publication date |
|---|---|
| FR869641A (en) | 1942-02-09 |
| NL58143C (en) | 1946-08-15 |
| CH223783A (en) | 1942-10-15 |
| DE715515C (en) | 1942-01-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2142564A (en) | Process for electrodeposition on aluminum and aluminum alloys | |
| US1968483A (en) | Plating aluminium and its alloys | |
| US3272728A (en) | Method of producing activated electrodes | |
| US2421863A (en) | Process for driving out occlusions of gases like hydrogen from the surface layers of workpieces | |
| US2347742A (en) | Pickling process | |
| US2835630A (en) | Treatment of metals prior to electro-plating | |
| US2457059A (en) | Method for bonding a nickel electrodeposit to a nickel surface | |
| US2389131A (en) | Electrodeposition of antimony | |
| US2811484A (en) | Electrodeposition of zinc on magnesium and its alloys | |
| US5456819A (en) | Process for electrodepositing metal and metal alloys on tungsten, molybdenum and other difficult to plate metals | |
| US2092130A (en) | Anodic cleaning process | |
| US3065154A (en) | Method of plating chromium and the like to titanium, its alloys, and the like | |
| US4055472A (en) | Method of preparing nickel alloy parts for plating | |
| US3915812A (en) | Method of manufacturing tinned plates having high corrosion resistant property | |
| US2241585A (en) | Process for removing metallic coatings from metallic parts | |
| JPH08176852A (en) | Roughening etching solution for platinum plating pretreatment of titanium and titanium alloy and roughening etching method for platinum plating pretreatment | |
| JPS61204393A (en) | Production of nickel coated stainless steel strip | |
| US2039328A (en) | Method for gold plating | |
| US3674655A (en) | Surface preparation of uranium parts | |
| JPS5911678B2 (en) | Manufacturing method of porous copper thin film | |
| US2884364A (en) | Method of electroplating on uranium | |
| EP0010989A1 (en) | Method of plating aluminium | |
| JPH0285394A (en) | Electroplating method of stainless steel plate | |
| US3645858A (en) | Silver plating baths | |
| US1198703A (en) | Process for obtaining adhesive coatings of copper upon iron and steel. |