GB659335A - Improvements relating to the electrodeposition of nickel - Google Patents
Improvements relating to the electrodeposition of nickelInfo
- Publication number
- GB659335A GB659335A GB10180/49A GB1018049A GB659335A GB 659335 A GB659335 A GB 659335A GB 10180/49 A GB10180/49 A GB 10180/49A GB 1018049 A GB1018049 A GB 1018049A GB 659335 A GB659335 A GB 659335A
- Authority
- GB
- United Kingdom
- Prior art keywords
- nickel
- electrolyte
- electrodeposition
- tank
- april
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/16—Regeneration of process solutions
- C25D21/18—Regeneration of process solutions of electrolytes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating And Plating Baths Therefor (AREA)
Abstract
659,335. Electrodeposition of nickel. MOND NICKEL CO., Ltd. April 14, 1949, No. 10180. Convention date, April 22, 1948. [Class 41] In electrodepositing nickel from a nickel sulphate electrolyte with the use of an insoluble anode, the nickel content of the electrolyte is replenished by passing direct current through it between soluble nickel electrodes under conditions such that the anode efficiency is substantially higher than the cathode efficiency, the current density lying between 1 and 25 amperes per square foot and the current being reversed at intervals of from 1 to 50 seconds, preferably at intervals of 3 to 7 seconds. The electrolyte may contain from 100 to 400 grams of nickel sulphate per litre and from 10 to 50 grams of boric acid per litre, may have a pH value of from 0.75 to 3.5 and may be at a temperature of from 38‹ to 71‹ C. The electrolyte is preferably continuously circulated between the electrodeposition tank and a replenishment tank, although electrodeposition and replenishment can be carried out in separate compartments of the same tank.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US22727A US2541721A (en) | 1948-04-22 | 1948-04-22 | Process for replenishing nickel plating electrolyte |
Publications (1)
Publication Number | Publication Date |
---|---|
GB659335A true GB659335A (en) | 1951-10-24 |
Family
ID=21811119
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10180/49A Expired GB659335A (en) | 1948-04-22 | 1949-04-14 | Improvements relating to the electrodeposition of nickel |
Country Status (4)
Country | Link |
---|---|
US (1) | US2541721A (en) |
FR (1) | FR984887A (en) |
GB (1) | GB659335A (en) |
NL (1) | NL71231C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4484704A (en) * | 1980-06-09 | 1984-11-27 | Raychem Corporation | Solder delivery system |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1262728B (en) * | 1952-07-19 | 1968-03-07 | Gen Am Transport | Device for carrying out a continuous chemical nickel plating process |
DE1145889B (en) * | 1952-07-19 | 1963-03-21 | Gen Am Transport | Process for the regeneration of continuously working baths for chemical nickel plating |
US2955944A (en) * | 1953-07-03 | 1960-10-11 | Gen Motors Corp | Electroless nickel plating bath control |
NL132272C (en) * | 1961-06-19 | |||
US3496082A (en) * | 1964-10-19 | 1970-02-17 | Ransburg Electro Coating Corp | Electrophoretic coating method and apparatus utilizing bath circulation to minimize impurities |
US3474011A (en) * | 1967-08-03 | 1969-10-21 | American Bank Note Co | Electroplating method and apparatus |
JPS585997B2 (en) * | 1979-01-25 | 1983-02-02 | 株式会社井上ジャパックス研究所 | electroforming equipment |
DE3144128C1 (en) * | 1981-11-06 | 1983-06-09 | Bayerische Motoren Werke AG, 8000 München | Device for the galvanic deposition of a metal on a metallic workpiece |
GB8911566D0 (en) * | 1989-05-19 | 1989-07-05 | Sun Ind Coatings | Plating system |
US5804053A (en) * | 1995-12-07 | 1998-09-08 | Eltech Systems Corporation | Continuously electroplated foam of improved weight distribution |
US6056862A (en) * | 1997-10-30 | 2000-05-02 | Daiki Engineering Co., Ltd. | Process and apparatus for supplying metal ions to alloy electroplating bath |
US6251255B1 (en) * | 1998-12-22 | 2001-06-26 | Precision Process Equipment, Inc. | Apparatus and method for electroplating tin with insoluble anodes |
WO2010043774A1 (en) * | 2008-10-14 | 2010-04-22 | Siemens Vai Metals Technolo Ies Sas | Method and installation for electrolytic tinning of a continuously running steel strip in an electrodeposition unit |
US8980068B2 (en) * | 2010-08-18 | 2015-03-17 | Allen R. Hayes | Nickel pH adjustment method and apparatus |
JP6139379B2 (en) * | 2013-10-31 | 2017-05-31 | 株式会社荏原製作所 | Sn alloy plating apparatus and Sn alloy plating method |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1003092A (en) * | 1907-04-11 | 1911-09-12 | Ontario Nickel Company Ltd | Method of electrolyzing nickel-sulfate solutions. |
US1144680A (en) * | 1914-05-23 | 1915-06-29 | Henry G Allers | Electroplating apparatus. |
GB310099A (en) * | 1928-01-26 | 1929-04-25 | George Lawton | Electro copper (or other metal similarly deposited) lined hollow drill steel, for goldmining and similar purposes |
US1885148A (en) * | 1929-09-13 | 1932-11-01 | Winchester Repeating Arms Co | Apparatus for electroplating |
US2431949A (en) * | 1943-11-24 | 1947-12-02 | Gen Motors Corp | Apparatus for electroplating the inside of bearing shells and the like |
US2449495A (en) * | 1944-01-12 | 1948-09-14 | Westinghouse Electric Corp | Application of phosphate protective coatings to nonferrous metals |
US2449422A (en) * | 1944-04-15 | 1948-09-14 | Harshaw Chem Corp | Electrodeposition of nickel |
NL69965C (en) * | 1945-08-10 | |||
NL72938C (en) * | 1947-07-09 | |||
DE3303930A1 (en) * | 1983-02-05 | 1984-08-09 | Basf Ag, 6700 Ludwigshafen | USE OF AQUEOUS POLY (METH) ACRYLATE SECONDARY DISPERSION AS A THICKENING Binder FOR COLORED STONE PLASTER |
-
0
- NL NL71231D patent/NL71231C/xx active
-
1948
- 1948-04-22 US US22727A patent/US2541721A/en not_active Expired - Lifetime
-
1949
- 1949-04-14 GB GB10180/49A patent/GB659335A/en not_active Expired
- 1949-04-21 FR FR984887D patent/FR984887A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4484704A (en) * | 1980-06-09 | 1984-11-27 | Raychem Corporation | Solder delivery system |
Also Published As
Publication number | Publication date |
---|---|
NL71231C (en) | |
US2541721A (en) | 1951-02-13 |
FR984887A (en) | 1951-07-11 |
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