US2088429A - Bright zinc - Google Patents
Bright zinc Download PDFInfo
- Publication number
- US2088429A US2088429A US68064A US6806436A US2088429A US 2088429 A US2088429 A US 2088429A US 68064 A US68064 A US 68064A US 6806436 A US6806436 A US 6806436A US 2088429 A US2088429 A US 2088429A
- Authority
- US
- United States
- Prior art keywords
- per gallon
- ozs
- zinc
- bright
- solution
- 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
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title description 19
- 229910052725 zinc Inorganic materials 0.000 title description 19
- 239000011701 zinc Substances 0.000 title description 19
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 10
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 8
- 238000000576 coating method Methods 0.000 description 8
- 229910017604 nitric acid Inorganic materials 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 6
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 229910052938 sodium sulfate Inorganic materials 0.000 description 5
- 235000011152 sodium sulphate Nutrition 0.000 description 5
- 238000005282 brightening Methods 0.000 description 4
- KXZJHVJKXJLBKO-UHFFFAOYSA-N chembl1408157 Chemical compound N=1C2=CC=CC=C2C(C(=O)O)=CC=1C1=CC=C(O)C=C1 KXZJHVJKXJLBKO-UHFFFAOYSA-N 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 3
- GTLDTDOJJJZVBW-UHFFFAOYSA-N zinc cyanide Chemical compound [Zn+2].N#[C-].N#[C-] GTLDTDOJJJZVBW-UHFFFAOYSA-N 0.000 description 3
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 2
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 2
- 239000004133 Sodium thiosulphate Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 2
- 239000004289 sodium hydrogen sulphite Substances 0.000 description 2
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 2
- 235000019345 sodium thiosulphate Nutrition 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F3/00—Brightening metals by chemical means
- C23F3/04—Heavy metals
- C23F3/06—Heavy metals with acidic solutions
Definitions
- the present invention relates to a method for producing zinc coated articles and more particularly to a bath which may beemployed to produce a bright finish on zinc plated articles.
- any plated zinc articles it is preferable however to form the initial zinc coating on a foundation metal in the following manner:
- the metal to be plated should be cleaned thoroughly and if it is an alloy high in carbon it may be found desirable to give it a sulphuric acid, anodic, electro-plating treatment.
- the cleaned article is then electroplated in a bath, the optimum composition of which is about ozs. per gallon of sodium cyanide, 8 to 10 ozs. per gallon of sodium hydroxide and 8 to 10 ozs. per gallon of zinc cyanide.
- a lower concentration of zinc cyanide results in a lower cathodic efliciency and better throwing power, but variations in the metal concentration do not affect the brightness and plating characteristics as markedly as variations in the sodium cyanide and caustic soda contents.
- Higher concentrations of sodium cyanide cause a decrease in cathodic efllciency and a slight increase in throwing power and a noticeable decrease in brightness.
- Higher and lower concentrations of caustic soda 'decrease cathodic efliciency and cause a darkening of the zinc plate.
- Any colloidal brightening agent may be added to the bath if desired but we have found sodium thiosulphate to be the most satisfactory, the optimum concentration employed being about oz.
- Sodium bisulphite up to about 4 cm. per gallon 45 may be added to the bath if desired and if the cyanide content of the bath is above the optimum value the addition of the sodium bisulphite reduces the cyanide content with a resultant increase in brightness of the plate.
- the optimum 50 current density range for a bright zinc deposit is from about 15 to 30 amperes' per square foot. The throwing power increases with higher current densities, with lower metal concentrations, or, in general, the factors which cause increased 55 cathodic polarization.
- the plated article is rinsed carefully and then dipped in a brightening solution which'consists substantially of 10 to 60 ozs. of chromic acidper gallon, .05 to 5 ozs. of anhydrous sodium sulphate per gallon and .1 to 1 oz. of nitric acid per gallon. After dipping the zinc plated article in this solution, it is again rinsed.
- the optimum values of the ingredients of the brightening bath are 40 ozs. of chromic acid per gallon, 2 ozs. per gallon of anhydrous sodium sulphate and .7 oz. per gallon of nitric acid.
- the resulting zinc coating does not stain and has a particularly bright and pleasing appearance.
- a solution adapted for the production of bright zinc surfaces said solution containing about 10 to 60 ozs. per gallon of chromic acid, about .05 to 5 ozs. per gallon of anhydrous sodium sulphate and about .1 to .1 oz. per gallon of nitric acid.
- a dipping solution for the production of bright zinc coatings consisting substantially of about 40 ozs. per gallon of chromic acid, 2 ozs. per gallon of anhydrous sodium sulphate and .7 oz. per gallon of nitric acid.
- the method of producing a bright zinc coating which comprises cleaning the article to be plated, immersing the cleaned article in a solution consisting of approximately 10 ozs. per gallon of sodium cyanide, 8 to 10 ozs. per gallon of sodium hydroxide, 8 to 10 ozs. per gallon of zinc cyanide and about A to 2 ozs. per gallon of sodium thiosulphate, maintaining the current density of about 15 to 30 amperes in said bath and thereafter immersing the zinc plated article in a brightening solution consisting substantially of 10 to 60 ozs. per gallon of chromic acid, .05 to 5 ozs. per gallon of anhydrous sodium sulphate and .1 to 1 oz. per gallon of nitric acid;
- a solution adapted for the production of bright zinc said solution containing 10 to 60 ozs. per gallon of chromic .acid, .1 to 1 oz. of nitric acid, and .05 to 5 ozs. per gallon of a compound containing a sulphate radical.
- a solution adapted for the production of bright zinc said solution containing chromic acid, nitric acid, and a compound containing a sulphate radical, the quantity of cromic acid varying from 10 to 60 ozs. per gallon, and the total quantity of said nitric acid and compound being materially less than the quantity of chromic acid present in said solution.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating And Plating Baths Therefor (AREA)
Description
Patented July 27, 1937 UlTE STAT s BRIGHT ZINC Walter E. Meyer, Milford, and Michael F. Dunleavey, Bridgeport, Conn., assignors to General Electric Company, a corporation of New York No Drawing. Application March 10, 1936, Serial No. 68,064
Claims.
The present invention relates to a method for producing zinc coated articles and more particularly to a bath which may beemployed to produce a bright finish on zinc plated articles.
5 Heretofore zinc in the form of an electro-plated coating, although offering a high resistance to oxidation, has been supplanted to a great extent by other and more expensive metals which offer a more attractive appearance. We have found however, that it is possible to produce a very .bright zinc coating which in appearance compares favorably with bright coatings of other and more expensive metals such as cadmium.
In carrying out our invention, we may employ any plated zinc articles. It is preferable however to form the initial zinc coating on a foundation metal in the following manner: The metal to be plated should be cleaned thoroughly and if it is an alloy high in carbon it may be found desirable to give it a sulphuric acid, anodic, electro-plating treatment. The cleaned article is then electroplated in a bath, the optimum composition of which is about ozs. per gallon of sodium cyanide, 8 to 10 ozs. per gallon of sodium hydroxide and 8 to 10 ozs. per gallon of zinc cyanide. A lower concentration of zinc cyanide results in a lower cathodic efliciency and better throwing power, but variations in the metal concentration do not affect the brightness and plating characteristics as markedly as variations in the sodium cyanide and caustic soda contents. Higher concentrations of sodium cyanide cause a decrease in cathodic efllciency and a slight increase in throwing power and a noticeable decrease in brightness. Higher and lower concentrations of caustic soda 'decrease cathodic efliciency and cause a darkening of the zinc plate. Any colloidal brightening agent may be added to the bath if desired but we have found sodium thiosulphate to be the most satisfactory, the optimum concentration employed being about oz. to the gallon, although amounts up to 2 ozs. per gallon have no detrimental effect. Sodium bisulphite up to about 4 cm. per gallon 45 may be added to the bath if desired and if the cyanide content of the bath is above the optimum value the addition of the sodium bisulphite reduces the cyanide content with a resultant increase in brightness of the plate. The optimum 50 current density range for a bright zinc deposit is from about 15 to 30 amperes' per square foot. The throwing power increases with higher current densities, with lower metal concentrations, or, in general, the factors which cause increased 55 cathodic polarization.
After the zinc coating has been plated on the foundation metal, the plated article is rinsed carefully and then dipped in a brightening solution which'consists substantially of 10 to 60 ozs. of chromic acidper gallon, .05 to 5 ozs. of anhydrous sodium sulphate per gallon and .1 to 1 oz. of nitric acid per gallon. After dipping the zinc plated article in this solution, it is again rinsed. The optimum values of the ingredients of the brightening bath are 40 ozs. of chromic acid per gallon, 2 ozs. per gallon of anhydrous sodium sulphate and .7 oz. per gallon of nitric acid. The resulting zinc coating does not stain and has a particularly bright and pleasing appearance.
What we claim as new and desire to secure by letters Patent of the United States, is:
1. A solution adapted for the production of bright zinc surfaces, said solution containing about 10 to 60 ozs. per gallon of chromic acid, about .05 to 5 ozs. per gallon of anhydrous sodium sulphate and about .1 to .1 oz. per gallon of nitric acid.
2. A dipping solution for the production of bright zinc coatings, said solution consisting substantially of about 40 ozs. per gallon of chromic acid, 2 ozs. per gallon of anhydrous sodium sulphate and .7 oz. per gallon of nitric acid.
3. The method of producing a bright zinc coating which comprises cleaning the article to be plated, immersing the cleaned article in a solution consisting of approximately 10 ozs. per gallon of sodium cyanide, 8 to 10 ozs. per gallon of sodium hydroxide, 8 to 10 ozs. per gallon of zinc cyanide and about A to 2 ozs. per gallon of sodium thiosulphate, maintaining the current density of about 15 to 30 amperes in said bath and thereafter immersing the zinc plated article in a brightening solution consisting substantially of 10 to 60 ozs. per gallon of chromic acid, .05 to 5 ozs. per gallon of anhydrous sodium sulphate and .1 to 1 oz. per gallon of nitric acid;
4. A solution adapted for the production of bright zinc, said solution containing 10 to 60 ozs. per gallon of chromic .acid, .1 to 1 oz. of nitric acid, and .05 to 5 ozs. per gallon of a compound containing a sulphate radical.
5. A solution adapted for the production of bright zinc, said solution containing chromic acid, nitric acid, and a compound containing a sulphate radical, the quantity of cromic acid varying from 10 to 60 ozs. per gallon, and the total quantity of said nitric acid and compound being materially less than the quantity of chromic acid present in said solution.
WALTER R. MEYER. MICHAEP F. DUNLEAVEY.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US68064A US2088429A (en) | 1936-03-10 | 1936-03-10 | Bright zinc |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US68064A US2088429A (en) | 1936-03-10 | 1936-03-10 | Bright zinc |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2088429A true US2088429A (en) | 1937-07-27 |
Family
ID=22080192
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US68064A Expired - Lifetime US2088429A (en) | 1936-03-10 | 1936-03-10 | Bright zinc |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2088429A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2434021A (en) * | 1943-03-08 | 1948-01-06 | Ncr Co | Process of bright dipping |
| US2477310A (en) * | 1947-07-23 | 1949-07-26 | Clark Thread Co | Process and composition for producing a dyeable corrosion resistant surface on zinc and high zinc alloys |
| US2502476A (en) * | 1948-06-02 | 1950-04-04 | Rheem Mfg Co | Producing transparent protective films on zinc or cadmium |
| US2634224A (en) * | 1949-12-22 | 1953-04-07 | Underwood Corp | Brightening and passivating solution |
-
1936
- 1936-03-10 US US68064A patent/US2088429A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2434021A (en) * | 1943-03-08 | 1948-01-06 | Ncr Co | Process of bright dipping |
| US2477310A (en) * | 1947-07-23 | 1949-07-26 | Clark Thread Co | Process and composition for producing a dyeable corrosion resistant surface on zinc and high zinc alloys |
| US2502476A (en) * | 1948-06-02 | 1950-04-04 | Rheem Mfg Co | Producing transparent protective films on zinc or cadmium |
| US2634224A (en) * | 1949-12-22 | 1953-04-07 | Underwood Corp | Brightening and passivating solution |
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