US2870070A - Electrodeposition of tin and electrolyte therefor - Google Patents

Electrodeposition of tin and electrolyte therefor Download PDF

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Publication number
US2870070A
US2870070A US672381A US67238157A US2870070A US 2870070 A US2870070 A US 2870070A US 672381 A US672381 A US 672381A US 67238157 A US67238157 A US 67238157A US 2870070 A US2870070 A US 2870070A
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United States
Prior art keywords
tin
electrolyte
electrodeposition
sulfamic acid
dihydroxydiphenylsulfone
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US672381A
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Richard F Higgs
Charles J Owen
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United States Steel Corp
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United States Steel Corp
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/30Electroplating: Baths therefor from solutions of tin
    • C25D3/32Electroplating: Baths therefor from solutions of tin characterised by the organic bath constituents used

Definitions

  • the sulfamic radical has heretofore been thought unsuitable for a tin-plating electrolyte, apparently because tin sulfamate is practically insoluble in water (Piontelli et al., The Use of Sulfamate Baths in Plating and Electrometallurgy, Chimica e Industria 21, 478).
  • Cupery Patent No. 2,318,592 significantly omits tin from the metals which may be deposited from sulfamate electrolytes.
  • a ductile, adherent coating of tin may be electroplated on steel from a solution of sulfamic acid and a tin salt, containing a suitable addition agent.
  • an electrolyte by dissolving sulfamic acid in water to a concentration of from 30 to 80 g./l. and add a stannous salt such as the sulfate in an amount sufficient to give from 15 to 50 g./l. of stannous ions.
  • a stannous salt such as the sulfate in an amount sufficient to give from 15 to 50 g./l. of stannous ions.
  • one of the reagents used in phenolsulfonic-acid electrolyte for tin-plating viz., diethyl, trimethyl or tetraethyl dihydroquinoline to a concentration of from .2 to 8 g./l.
  • stannous fluoborate may be used in amounts providing a corresponding concentration of tin ions.
  • the strip may have a speed of from 200 to 1000 F. P. M.
  • the strip should preferably be in contact with the solution for from 5 to 15 seconds, depending on the current density and the amount of plating desired.
  • the addition agent dihydroquinoline, dihydroxydiphenylsulfone, bispara-hydroxyphenyl propane or dihydroxybenzophenone serves to make the deposited tin layer brighten when melted by subsequently heating the base metal.
  • the electrolyte of our invention makes it possible to deposit a smooth adherent layer of tin.
  • the electrolyte is easy to make up, has a high conductivity permitting high current densities to be maintained, and will tolerate contamination by various impurities.
  • the tin layer deposited therefrom is ductile as well as adherent, and brightens when melted.
  • sulfamic acid in the electrolyte has several important advantages. It is solid, non-hygroscopic and nonvolatile, and is therefore easy to ship and handle. It is less corrosive than sulfuric acid, is very soluble in water and is highlyionized in solution. Sulfamic acid is available commercially at prices lower than phenolsulfonic acid and is safer to handle than sulfuric acid.

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  • 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)

Description

ELECTRODEPOSITION F TIN AND ELECTROLYTE THEREFGR Richard F. Higgs and (Iharles J. Owen, Pittsburgh, Pa.,
assignors to United States Steel Corporation, a corporation of New Jersey No Drawing. Applieation July 17, 1957 Serial No. 672,381
2 Claims. (Cl. 204-54) the method involving the use thereof. According to the invention, we provide an electrolyte containing sulfamic acid and tin ions as well as an addition agent. The addition agent is a water-soluble organic compound which causes the deposited tin to form a layer which brightens when melted.
The sulfamic radical has heretofore been thought unsuitable for a tin-plating electrolyte, apparently because tin sulfamate is practically insoluble in water (Piontelli et al., The Use of Sulfamate Baths in Plating and Electrometallurgy, Chimica e Industria 21, 478). Cupery Patent No. 2,318,592 significantly omits tin from the metals which may be deposited from sulfamate electrolytes. We have found, however, that a ductile, adherent coating of tin may be electroplated on steel from a solution of sulfamic acid and a tin salt, containing a suitable addition agent.
In a preferred practice, we prepare an electrolyte by dissolving sulfamic acid in water to a concentration of from 30 to 80 g./l. and add a stannous salt such as the sulfate in an amount sufficient to give from 15 to 50 g./l. of stannous ions. To this solution we further add one of the reagents used in phenolsulfonic-acid electrolyte for tin-plating, viz., diethyl, trimethyl or tetraethyl dihydroquinoline to a concentration of from .2 to 8 g./l. As alternatives, we may use dihydroxydiphenylsulfone or hisparahydroxyphenyl propane. Dihydroxybenzophenone may be substituted for any of the above addition agents to a concentration of 2 to 10 g./l.
The following formula is one specific example of our electrolyte:
Water in desired quantity plus 50'g./l. sulfamic acid 64 g./l. stannous sulfate 5 g./l. dihydroxydiphenylsulfone Instead of the sulfate, other salts such as stannous fluoborate may be used in amounts providing a corresponding concentration of tin ions.
Using an electrolyte as above, we immerse a steel article such as thin strip or a sheet therein and make it the States Patent ice cathode with a current density of about 250 a. s. f. The temperature of the bath should be about F. The current density may, however, vary between 150 and 500 a. s. f. and the temperature between 90 and F If the treatment is continuous, as in ordinary commercial production, the strip may have a speed of from 200 to 1000 F. P. M. The strip should preferably be in contact with the solution for from 5 to 15 seconds, depending on the current density and the amount of plating desired. The addition agent (dihydroquinoline, dihydroxydiphenylsulfone, bispara-hydroxyphenyl propane or dihydroxybenzophenone) serves to make the deposited tin layer brighten when melted by subsequently heating the base metal.
The electrolyte of our invention makes it possible to deposit a smooth adherent layer of tin. The electrolyte is easy to make up, has a high conductivity permitting high current densities to be maintained, and will tolerate contamination by various impurities. The tin layer deposited therefrom is ductile as well as adherent, and brightens when melted.
The use of sulfamic acid in the electrolyte has several important advantages. It is solid, non-hygroscopic and nonvolatile, and is therefore easy to ship and handle. It is less corrosive than sulfuric acid, is very soluble in water and is highlyionized in solution. Sulfamic acid is available commercially at prices lower than phenolsulfonic acid and is safer to handle than sulfuric acid.
Although we have disclosed herein the preferred practice of our invention, we intend to cover as well any change or modification therein which may be made without departing from the spirit and scope of the invention.
We claim:
1. As an electrolyte for tin plating, a water solution containing from 30 to 80 g./l. of sulfamic acid, from 15 to 50 g./l. of stannous ions, and from .2 to 10 g./l. of an addition agent selected from the group consisting of diethyl, trimethyl, tetrainethyl dihydroquinoline, dihydroxydiphenylsulfone, bisparahydroxyphenyl propane, and dihydroxybenzophenone.
2. In a method of tin-plating on steel, the steps of immersing an article of steel in an electrolyte consisting substantially of water, from 30 to 80 g./l. of sulfamic acid, from 15 to 50 g./l. of stannous ions and from .2 to 10 g./1. of an addition agent selected from the group consisting of diethyl, trimethyl, tetramethyl dihydroquinoline, dihydroxydiphenylsulfone, bisparahydroxyphenyl propane, and dihydroxybenzophenone and making the article cathode with a current density of from to 500 a. s. f.
References Cited in the file of this patent UNITED STATES PATENTS 2,552,920 Allen May 15, 1951 FOREIGN PATENTS 756,788 Great Britain Sept. 12, 1956 OTHER REFERENCES Piontelli et al.: La Chimica e lIndustria, vol. 21 (1939), pp. 478-491..

Claims (1)

1. AS AN ELECTROLYTE FOR TIN PLATING, A WATER SOLUTION CONTAINING FROM 30 TO 80 G./L. OF SULFAMIC ACID, FROM 15 TO 50 G./L. OF STANNOUS IONS, AND FROM .2 TO 10 G./L. OF AN ADDITION AGENT SELECTED FROM THE GROUP CONSISTING OF DIETHYL, TRIMETHYL, TETRAMETHYL DIHYDROQUINOLINE, DIHYDROXYDIPHENYLSULFONE, BISPARAHYDROXYPHENYL, PROPANE, AND DIHYDROXYBENZOPHENONE.
US672381A 1957-07-17 1957-07-17 Electrodeposition of tin and electrolyte therefor Expired - Lifetime US2870070A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2976169A (en) * 1958-02-12 1961-03-21 Du Pont Immersion deposition of tin
US3471379A (en) * 1965-02-13 1969-10-07 Philips Corp Tin plating baths
US3479259A (en) * 1966-12-30 1969-11-18 Enthone Bright,level tin plating

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2552920A (en) * 1947-08-27 1951-05-15 United States Steel Corp Electrolytic tin plating bath
GB756788A (en) * 1954-05-27 1956-09-12 Cyril James Faulkner Electro-tinning process

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2552920A (en) * 1947-08-27 1951-05-15 United States Steel Corp Electrolytic tin plating bath
GB756788A (en) * 1954-05-27 1956-09-12 Cyril James Faulkner Electro-tinning process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2976169A (en) * 1958-02-12 1961-03-21 Du Pont Immersion deposition of tin
US3471379A (en) * 1965-02-13 1969-10-07 Philips Corp Tin plating baths
US3479259A (en) * 1966-12-30 1969-11-18 Enthone Bright,level tin plating

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