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Publication numberUS3260580 A
Publication typeGrant
Publication dateJul 12, 1966
Filing dateNov 19, 1962
Priority dateNov 19, 1962
Publication numberUS 3260580 A, US 3260580A, US-A-3260580, US3260580 A, US3260580A
InventorsKamm Gilbert George, Willey Allen Ray
Original AssigneeAmerican Can Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Tin plate having a tin-nickel-iron alloy layer and method of making the same
US 3260580 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)


lllllllll A Tra/QA/fys United States Patent O TIN PLATE HAVING A TiN-NICKEL-lRON ALLOY LAYER AND METHOD F MAKING THE SAME Gilbert George Kamm, Barrington, and Allen Ray Willey,

Mundelein, Ill., assignors to American Can Company,

New York, NY., a corporation of New .Hersey Filed Nov. 19, 1962, Ser. No. 238,698 13 Claims. (Cl. 29-196A) This invention relates to coated ferrous metal sheet yand the method of making the same. More particularly, the invention pertains to ferrous metal sheet covered with a composite coating comprising an outer layer of tin and an intermediate layer of a tin-nickel-iron lalloy between the ferrous metal sheet and the tin outer coating, and to the method of making lthe same.

Although the conventional tin can, which is essentially made of sheet steel covered with a thin layer of metallic tin, has proved very effective as a container for corrosive products, there have been continuing efforts over the years to improve the corrosion resistance of the cans in order to increase the length of time that corrosive products may be sealed within the containers without spoilage of the product.

With the advent of the electrotinning process for coating steel sheet, rather than the hot dip method, the thickness of the tin deposit has decreased significantly. This in turn has increased the susceptibility -of the material to corrosion by the products within cans made from the sheet.

Based upon various tests, tin plate having superior corrosion resistance is designated grade A plate, whereas tin plate having average corrosion resistance is designated grade B plate. It follows that a large number of products packed in cans made from grade A plate have a longer shelf or storage life than in cans made tfrorn grade B plate. The present invention is especially concerned wit-h the simpler production of plate which consistently has corrosion resistance equal to 4or better than commercial .grade A plate.

It is therefore an object of this invention to provide a coated steel that will have superior corrosion resistance .and a method for making such a material.

Another object is to provide a composite coated ferrous metal sheet for use in the manufacture of metal containers.

An additional object is to provide a ferrous metal sheet having thereon uniformly thin coating layers which increase the corrosion resistance of the sheet.

A further object of this invention is to provide tin plate having corrosion resistance equal to or -better than present-day commercial grade A plate even though the tin is deposited from an acid tin plating bath.

A still further object is to provide a corrosion-resistant tin plate which gives cans made therefrom a longer storage or shelf life when packed with products which corrode the can.

Yet another object is to provide a relatively simple and -less expensive method of making tin plate having irnproved corrosion resistance which may be readily incorporated into present-day, commercial tin plate production.

Numerous other objects and advantages of the invention will be apparent `as it is better understood from the following descrip-tion, which, taken in connection with the accompanying drawings, disclose a preferred embodiment thereof.

The .above and other objects of `the present invention are obtained by providing a ferrous basis metal sheet having thereon an outer coating of flow-brightened tin and a tin-nickel-iron alloy layer between the tin outer 3269,53@ Patented July l2, i966 ice coating and the Aferrous basis metal. rI'his ternary alloy is obtained by the co-deposition of tin and nickel over the basis metal and thereafter depositing a layer of t-in over the intermediate tin-nickel layer. Subsequently the coated sheet is heated to a temperature sufficient -to melt the deposited tin coating and alloy a portion of the basis ferrous metal land tin with the vdeposited binary alloy coating, thus forming a composite sheet having a bright tin outer coating and a ternary Sn-Ni-Fe alloy intermediate alloy.

Referring to the drawings:

FIG. l is a perspective view of a container made from the material of Ithis invention.

FIG. 2 is an enlarged fragmentary sectional view taken substantially along line 2-2 of FIG. 1.

As a preferred or exa-mplary embodiment of the present invention, FIG. l illustrates a metal container, generally designated 20, 'having a body 22, and upper and lower ends thereon 23, 24 respectively, made integral with the body 22 by any suitable means such as upper and lower double seams 25, 26 respectively.

The material, from which the container is made, is a composite coated metal sheet having a tin-nickel-iron ternary alloy 32, lying between an outer bright tin coating 34 and a ylow carbon ferrous basis metal 36 (FIG. 2).

it may sometimes be desirable to coat the inner surface of the container 20 with a synthetic resin 38. This would, of course, depend upon the product to be packaged. Among many resins that may be utilized `for this purpose are phenolics, epoxies, crganosols, vinyls, etc.

The tin-nickel-iron ternary alloy 32 is a thin, substantially continuous layer formed by diffusing a tin-nickel intermediate layer with the basis metal 36 and an asdeposited or .matte tin coating, by a method which will be described more `fully hereinafter.

Thickness of the ternary yalloy 32 will range from 0.25 X10*6 to 8X106 inch, with a thickness of 1 10r6 to i6 l0t6 inch preferred. Although the thickness of the alloy is very small, it is thought that its uniformity and excellent coverage of the basis metal l3,6, together with its metallurgical composition, results in increased ,corrosion resistance of the composite sheet when cornpared to conventional tin plate.

Tin plate made according to conventional procedures generally shows that neither the bright outer tin 'layer nor the tin-iron alloy layer lying between the tin and the steel basis metal are completely continuous. In other words, voids or discontinuities exist in each of these layers. Some of the voids in each layer are in alignment, so that through them basis steel is exposed to the environment in contact with the tin plate. Obviously, the more discontinuous either layer is, the greater the incidence of alignment and consequently the greater the amount of basis steel exposed. These exposed `areas of base steel are, in some products, vulnerable to direct corrosive attack, while in others they accelerate corrosion of tin from the plate surface.

In the present invention the Sn-Ni-Fe alloy layer is substantially contin-uous over the ferrous metal surface, thus obviating the discontinuity usually encountered with the Sn-Fe alloy layer in conventional tin plate. It is thought that this continuity is primarily due to the presence of nickel in the alloy, which acts to promote uniform nucleation during flow brightening of the as-deposited tin coating, which process will be described in more detail hereinafter.

The composite metal of this invention is produced by providing low carbon ferrous metal sheet, preferably in coil form, which is electrolytically cleaned in a hot alkaline cleaning solution, by means well known to those skilled in the art. Thereafter the strip is pickled in a 5% 3 sulfuric acid solution to remove any oxides present on the metal surface.

Once the surface contamination has been removed by cleaning and pickling, the strip is rinsed and then immersed in a tin-nickel plating bath having the fol-lowing nominal composition:

Ammonium hydroxide to pH 2.5.

Using the above tin-nickel alloy plating solution, a steel sheet, cleaned and pickled according to the method hereinbefore describe-d, was immersed in the electrolyte, Whose temperature was maintained at 150 F. A direct current at a density of 25 amperes per square foot was then passed through the electrolyte for 2 seconds, while Iagitation of the solution was kept at a minimum. A total current of 50 ampere-seconds per square foot was thus passed, -resulting in a tin-nickel alloy deposit having a thickness of approximately 1.1 -6 inch.

Alloy anodes -may be used in the plating operation. However, the usual proced-ure, which is what was used in the example, is to employ separate anodes of tin and nickel, using one tin anode for each two nickel anodes. An alternate method is to use `only nickel anodes and to maintain the tin concentration in the bath through the periodic addition of anhydrous stannous chloride. Deposition carried out at a current density of from amperes per square foot (asf.) to 600 asf., depending upon the degree of solution agitation, at a temperature of approximately 150 F.

During the coplating operation, the current is passed for a time of 0.025 to 10 seconds, With an optimum plating time of 1 to 4 seconds and 2 seconds preferred. It is readily apparent that the plating time will vary according to the current density employed. This Will give a deposit having a nominal composition of 65% tin and nickel. This composition has the nominal atomic percentage of Sn-Ni, with the deposited composition remaining substantially constant over a Wide range of operating conditions and solution variables.

The Sn-Ni thickness will range from 0.275 10-s inch to 5.5 106 inch, With a preferred deposit thickness of 1.l 106 inch. The thickness range may be produced by passing from 6.25 to 250 ampere-seconds of current per sq. ft.

Although electroplating of the alloy coating is preferred, primarily for economic reasons, other techniques such as vacuum deposition or gaseous deposition may be used.

Subsequent to the deposition of Sn-Ni the strip is rinsed and then immersed in a tin plating bath. Either an alkaline or acid tin plating bath may be used, but the acid type is considered more desirable due to the higher current densities that may be used, and consequently the shorter plating cycles that may be attained.

One of numerous acid tin plating baths that may be used has a composition as follows:

Oz. per gal. Stannous sulfate 13 Sulfuric acid 4 Tartaric acid 4 Animal glue 0.4-0.8 Cresol or 0.8 B-napthol 0.13

The bath is operated at room temperature and pure tin `anodes are used in order to minimize the formation of sludge during plating. i

Using a current density of from 10 to 400 a.s.f., dependent upon the degree of agitation in the bath, a coating of tin from 10X10*6 to 90x106 inch in thickness is deposited upon the intermediate Sn-Ni layer. Preferably the tin deposit will have a thickness from 30 10 6 to 60x10*6 inch.

It is possible to deposit the tin coating by such techniques as vacuum or gaseous deposition, although the hereinbefore mentioned electrolytic method is preferred.

Once the composite coating has fbeen deposited upon the ferrous -metal strip, the next operation in the process is to flow brighten the lcoating and thereby produce a bright tin surface, in addition to transforming the intermediate Sn-Ni alloy coating to a Sn-Ni-Fe ternary alloy.

Either resistance or induction heating may `be used to heat the coated strip. By means of either heating method the coated metal is heated to a temperature ranging from 450 F., the melting point of tin, to approximately 550 F. The temperature is maintained above 450 F. for a period of 0.01 to 1 second, and preferably 0.25 second.

The flow brightening step causes the tin to flow out into a smooth, bright film and to ybecome rmly anchored to the alloy layer. In addition, the heating during flow brightening results in the formation of the tin-nickel-iron ternary alloy which lies between the bright tin outer coating and the ferrous 'basis metal.

Although not wishing to be `bound by any particular theory as to the reaction in forming the ternary alloy layer during flow brightening, it is thought that some of the melted tin diffuses into the tin-nickel alloy and then some surface iron in contact with the tin-nickel alloy combines with the binary alloy in a second diffusion reaction. The diffusion reactions may proceed simultaneously. During the diffusion process the nickel, in the now ternary alloy, functions as centers for nucleation, thus resulting in uniform nucleation and a uniform alloy layer.

Although satisfactory results are obtainable by flow brightening the tin at temperatures substantially above its melting point, for best results, both as to appearance and corrosion resistance, the tin should -be fiowed at temperatures above, but as close as possible to, the melting point of tin. It is preferred that the tin remain at the temperature above its melting point for as short a time as possible. To this end, the molten tin is solidified as rapidly as possible, such as by a cool air bath or a water quench or both.

One test which is used in determining the quality of tin plate is the alloy-tin-couple test or, as it is most cornmonly called, the ATC test. Attention is given to the electrochemical factors important to tin plate corrosion in this test in which steel is protected from corrosion by coupling with tin. The rate of detinning or corrosion is determined -by the galvanic couple current and is measured in microamperes per square centimeter. ATC measurements for typical electrolytic tin plate will generally range from 0.02 to 0.30 microampere per square centimeter, with the grade A plate having the lower values and grade B plate, usually resulting from commercial acid tin plating procedures, having the higher values. When tin plate made according to the present invention, even plate on which the tin was deposited from an acid plating bath, was subjected to the ATC test, the values ranged from only 0.015 to 0.050 microampere per square centimeter. Thus, with plate made according to this invention, -it is possible to obtain ATC values even lower than for conventional grade A tin plate.

It is thought that the invention and many of its attendant advantages will be understood from the foregoing description, and it will be apparent that various changes may be made in the form, construction and arrangement of the parts and that changes may -be made in the steps of the method described and the order of accomplishment without departing from the spirit and scope of the invention or sacrificing all of its material advantages, the form hereinbe'fore described being merely a preferred embodiment thereof.

We claim:

1. A coated ferrous metal sheet, comprising: a ferrous basis metal; an inner coating over and in contact with said basis metal consisting essentially of a ternary alloy of tin, nickel, and iron; and an outer coating of tin over and in contact with said ternary alloy, said ternary alloy being produced by the diiusion of an intermediate deposit of a binary tin-nickel alloy with said ferrous basis metal and said outer tin coating while said tin coating is molten.

2. The sheet of claim 1 wherein said ternary alloy coating has a thickness from 0.25)(-6 to 8X106 inch.

3. The sheet of claim 2 wherein said ternary alloy coating has a thickness from 1x10"6 to 6x10*6 inch.

4. The sheet of clairn 2 wherein said outer tin coating has a thickness from 10X106 to 90x10-6 inch.

5. A method of manufacturing a composite coated ferrous metal sheet, comprising the steps of: depositing a layer of a tin-nickel binary alloy on a ferrous basis metal sheet; maintaining said binary alloy substantially in its as deposited condition while depositing a layer of tin over said -binary alloy, said tin deposit having a thickness greater than said deposit of tin-nickel alloy; heating said coated ferrous sheet to a temperature above `450 F., for a time sufficient to melt said tin coating and to diffuse iron from said basis metal into throughout said binary alloy while said -basis metal and said binary alloy are solid to form a tin-nickel-iron ternary alloy over and in contact with said basis metal; and thereafter cooling said coated sheet to a temperature below the melting point of tin to solidify said tin as a surface coating over and in contact with said ternary alloy.

6. The method of claim 5 wherein said tin-nickel alloy is electrodeposited.

7. The method of claim 5 wherein said tin-nickel alloy is deposited to a thickness from 0.275 X10s to 5.5 10*s inch.

8. The method of claim 5 wherein said tin is electrodeposited.

9. The method of claim 5 wherein said tin is deposited to a thickness from 10X10*6 to 90 106 inch.

10. The method of claim 5 wherein said ternary alloy has a thickness from 0.25 X10*G to 8X106 inch.

11. The method of claim 5 wherein said bright tin has a thickness from 10X106 to 90 10d6 inch.

12. The method set forth in claim 5 wherein said coated ferrous sheet is maintained at said temperature above 450 F. for a period of from 0.01 to 1 second.

13. The method set forth in claim 12 wherein said coated ferrous sheet is maintained at a temperature 'between 450 F. and 550 F.

References Cited by the Examiner UNITED STATES PATENTS 2,085,543 6/1937 opiinger 2044-40 2,266,330 12/1941 Nachiman 204-375 2,428,318 9/1947 Naehtman 204-375 2,775,535 12/1956 Poole 204-37.5 2,914,449 11/1959 Mayer 204-43 3,062,726 11/1962 Hin 204-375 WINSTON A. DOUGLAS, Primary Examiner. MURRAY TILLMAN, Examiner. L. G. WISE, H. S. WILLIAMS, Assistant Examiners.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2085543 *May 21, 1935Jun 29, 1937Du PontProcess for coating metals
US2266330 *Feb 25, 1937Dec 16, 1941John S NachtmanProcess for electroplating strip steel
US2428318 *Mar 9, 1942Sep 30, 1947John S NachtmanElectrolytic deposition of rustproof coatings
US2775535 *Mar 14, 1952Dec 25, 1956Bethlehem Steel CorpTreatment of tinplate
US2914449 *May 19, 1954Nov 24, 1959Int Standard Electric CorpLow resistance contacts to germanium
US3062726 *Aug 21, 1958Nov 6, 1962Inland Steel CoElectrolytic tin plate production
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3334030 *Apr 10, 1964Aug 1, 1967Jones & Laughlin Steel CorpProduction of electrolytic tinplate
US3445351 *Oct 21, 1964May 20, 1969Du PontProcess for plating metals
US3620934 *Jul 19, 1967Nov 16, 1971Fer Blanc Sarl Centre Rech DuMethod of electrolytic tinning sheet steel
US4015950 *Aug 1, 1975Apr 5, 1977Agence Nationale De Valorisation De La Recherche (Anvar)Surface treatment process for steels and article
US4104135 *Aug 4, 1975Aug 1, 1978Kawasaki Steel CorporationDiffusion of nickel, copper, or nickel-tin alloy coating into shee before plating
US5094924 *Jun 1, 1990Mar 10, 1992Kenzo MatsuiPolyester resin film laminated steel sheet for drawn and ironed can
US5993994 *Oct 3, 1994Nov 30, 1999Toyo Kohan Co., Ltd.Surface treated steel sheet for battery containers, a battery container, and a battery produced thereof
US8487183 *May 12, 2009Jul 16, 2013Phoenix Contact Gmbh & Co. KgContact unit and method for producing a contact unit
US20100314157 *May 12, 2009Dec 16, 2010Phoenix Contact Gmbh & Co. KgContact unit and method for producing a contact unit
U.S. Classification428/648, 428/935, 427/405, 205/252, 205/152, 428/938, 427/383.7, 205/95, 427/409, 427/250, 205/236, 428/926, 428/678
International ClassificationC23C10/34, C25D5/10
Cooperative ClassificationB65D7/00, Y10S428/938, Y10S428/935, Y10S428/926, C25D5/10
European ClassificationB65D7/00, C25D5/10