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US2088429A - Bright zinc - Google Patents

Bright zinc Download PDF

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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
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United States
Prior art keywords
per gallon
ozs
zinc
bright
solution
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Expired - Lifetime
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US68064A
Inventor
Walter R Meyer
Michael F Dunleavey
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
General Electric Co
Original Assignee
General Electric Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by General Electric Co filed Critical General Electric Co
Priority to US68064A priority Critical patent/US2088429A/en
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Publication of US2088429A publication Critical patent/US2088429A/en
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Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23FNON-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
    • C23F3/00Brightening metals by chemical means
    • C23F3/04Heavy metals
    • C23F3/06Heavy 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.

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  • 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.
US68064A 1936-03-10 1936-03-10 Bright zinc Expired - Lifetime US2088429A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Cited By (4)

* Cited by examiner, † Cited by third party
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

Cited By (4)

* Cited by examiner, † Cited by third party
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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