GB299725A - - Google Patents
Info
- Publication number
- GB299725A GB299725A GB31374/28A GB3137428A GB299725A GB 299725 A GB299725 A GB 299725A GB 31374/28 A GB31374/28 A GB 31374/28A GB 3137428 A GB3137428 A GB 3137428A GB 299725 A GB299725 A GB 299725A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- colloidal
- addition
- electrolyte
- zinc
- 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
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Glass Melting And Manufacturing (AREA)
- Silicon Compounds (AREA)
Abstract
299.725. Metallges. Akt.-Ges., (formerly Metallbank und Metallurgische Ges.). Oct. 27, 1927, [Convention date]. Copper, zinc, and other metals, depositing.- Smooth and dense deposits of metals are obtained by the addition to the bath of a hydrophilic inorganic colloid insoluble in the electrolyte in the absence of oxidizing agents akin to hydrogen peroxide care is taken that the colloidal material enters the cell in the required state of dispersion and that detrimental substances are not introduced with it. The colloidal material is not extracted from an ore in the formation of the electrolyte. The colloidal material should be added in very dilute form either continuously or in small amounts at short intervals. In electrolyzing solution obtained by leaching zinc oxide not containing silica with acid zinc sulphate solution the addition may consist of 0.25 gms. per litre of colloidal silicic acid obtained by mixing zinc silicate with a multiple of the amount of sulphuric acid required for decomposition. Smaller additions are necessary when the zinciferous material already contains silicic acid. The zinc silicate may be precipitated by the addition of water glass to neutral regenerated electrolyte, and the colloidal silicic acid obtained from the separated precipitate by addition of spent electrolyte. Alternatively an alkaline earth silicate may be employed as the source of silica. In the refining of copper, the colloidal addition may consist of hydrated tunstic acid obtained from copper tungstate by the addition of an equivalent amount of sulphuric acid. Metatitanic acid or zirconic acid may be employed as colloidal additions in the case of acid electrolytes, and ferric hydroxide or magnesium hydroxide in the case of alkaline electrolytes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE299725T | 1927-10-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB299725A true GB299725A (en) | 1929-11-28 |
Family
ID=31894226
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31374/28A Expired GB299725A (en) | 1927-10-27 | 1928-10-29 |
Country Status (2)
Country | Link |
---|---|
BE (1) | BE355258A (en) |
GB (1) | GB299725A (en) |
-
0
- BE BE355258D patent/BE355258A/xx unknown
-
1928
- 1928-10-29 GB GB31374/28A patent/GB299725A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
BE355258A (en) |
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