US2384086A - Method of making tin plate - Google Patents

Method of making tin plate Download PDF

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US2384086A
US2384086A US310650A US31065039A US2384086A US 2384086 A US2384086 A US 2384086A US 310650 A US310650 A US 310650A US 31065039 A US31065039 A US 31065039A US 2384086 A US2384086 A US 2384086A
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strip
tin plate
tin
metal
coating
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US310650A
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Charles E Glock
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Crown Cork and Seal Co Inc
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Crown Cork and Seal Co Inc
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/48After-treatment of electroplated surfaces
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/4998Combined manufacture including applying or shaping of fluent material
    • Y10T29/49982Coating

Definitions

  • This invention is an improved tin plate and I method for preparing'same.
  • One object of the invention is to provide tin plate with a tin coating having enhanced rust resistance.
  • Another object of the invention is to provide tin plate with a surface of increased hardness.
  • the hardness characteristic renders the prodresistant and materially lessens the likelihood of scratching and incipient oxidation of the base.
  • a further object of the invention is to produce tin plate having a higher lustre and smoothness as compared with tin plate heretofore available. Since tin plate is employed frequently because it is desired to give a nice appearance to an article, the presence of a surface having an lmproved polish is very desirable.
  • An additional object of the invention is to produce tin plate having an increased affinity for lithograph and printing inks as well as decorative and protective lacquers and paints.
  • Such coatings are frequently applied to tin boxes, cans, container closures and other marked distinction to hot-dip tin plate which lraeggise of the presence of oily residue frequently e s a coa mg or allows the rubbed on same to be readily
  • Another object of the invention is to provide tin plate having enhanced temper and workability. That is to say, the tin plate of this invention can be fabricated, as by stamping, drawing or other metal working operations into various shapes without danger of the metal cracklng or of the tin coating peeling or flaking from the metal base.
  • This method embodies a combination of steps comprising (1) electrolytically coating the base metal with tin followed by (2) a skin pass treatment in the nature of a high presure cold-rolling.
  • An additional object of the invention is to provide a method wherein continuous base metal strip or sheets of increased width, as compared to sheets platable by methods heretofore available, may be tin plated with facility.
  • base metal having a width of 30 inches or more may be readily plated by the method of the present .invention. purposes, ability to increase the width of the tin plate affords a substantial economy, as in the manufacture of container closures and containers.
  • the reduction in the first pass should be at least of one percent, which may be increased as desired. So far as the brightness of the coating is concerned, I have found no objectionable maximum reduction below which the reduction must be maintained in the first pass. However, it is desirable that the reductionnot reach a point where the strip is objectionably deformed as indicated by bowing or wrinkling. Consequently, the percentage of reduction in the first pass should be maintained below that which will cause such strip deformation. Subsequent passes do not destroy the effects obtained in the appearance of the metal when the elongation or reduction in the first pass is controlled in this manner.
  • the rolls of the mill should be adjusted to apply a pressure of'the order of from at least 250,000 to 500,000 lbs.
  • a pressure of'the order of from at least 250,000 to 500,000 lbs Such a range of For many finish and coincident reduction when rolling, for example, a strip 30 inches wide and having a gauge of approximately .011 inch.
  • This pressure may be determined inthe conventional way, by an instrument employed to register the elongation of the mill housing during the application of pressure. Suchinstruments are well known and are employed on substantially all types of rolling mills. The particular figures given were taken from such instrument applied to a 4-high Mesta tempering mill. When so controlled, the elongation and gauge reduction is of the order above recited.
  • the metal may be fed through the mill at a rate of from 1200 to 2000 feet per minute.
  • Figure 2 is 'a diagrammatic illustration of the cold-rolling step
  • Figure 3 is a diagrammatic view showing the manner in which'the electro-coated band is continued to the cold-rolling instrumentality.
  • the customary steel or black iron of appropriate gauge is utilized.
  • the metal is usually annealed and is supplied in continuous strips in the form of rolls by the steel mill,
  • the numeral ll indicates an apparatus for welding ends of the strips together and the numeral l2 indicates a table having a holding clamp to maintain one end of the strip during the welding operation.
  • the numeral l3 indicates the acid pickling tank which generally contains hydrofluoric or other suitable acid while the numeral N indicates a cold water rinsing tank.
  • the strip I just prior to entering the electrolytic both I5 is heated by means of steam jets I6 to a temperature of about 160 F.
  • the heating means employed namely, steam application is of a character which will not dry the surface of the strip; ,there is suflicient condensation of the steam to maintain 2,884,086 7 the desired protective moist film.
  • the strip is fed through the'bath at varying speeds which may be as high as 500 feet a minute or greater. It will be noted that in the bath the strip is coated while traveling in vertically disposed position.
  • the chemical reagents employed are preferably sodium stannate 5.4 ounces to 13 ounces; sodium acetate 2 ounces to 5 ounces; and caustic soda 1 ounce to 3 ounces, per-gallon of water.
  • sodium cyanide is included in the bath in an amount to insure that the electrodes corrode uniformly, for example, about 1 ounce to 6 ounces, per gallon of water.
  • the current density is maintained between 10 and '75 amperes per square foot of cathode (strip) and the temperature of the bath is. generally substantially between 158 to 200 F.
  • the weight of the coating may be controlled by varying the time to which the strip is subjected to the bath as by regulating the speed of travel of the strip or by varying the amperage or by doing both.
  • the coated strip is led through a cold water rinsing tank l8 and then through a hot water rinsing tank 19 whereupon it travels through a tensioning mechanism 20 and is wound into coils 2i.
  • the coated metal is dull and soft and will have a thickness or weight of tin coat controlled in accordance with the use to be made of the tin plate.
  • the coils of coated metal are each transferred to a suitable uncoiler for continuously'feeding the strip to the cold-rolling instrumentality which is in the form of a usual a-ihigh mill as shown'at 22 in Figure 2.
  • the coated sheet is given a skin, pass treatment by means of a high pressure cold-rolling to impart thev properties of rust resistance, smoothness, hardness, temper and workability, and high lustre in a manner appreciably better than present available tin plate now possesses.
  • the apparatus disclosed has the rolls rotating at uniform speed.
  • the improved polish or high lustre of the tin plate is appreciable and 'very materially enhances the appearance of the product.
  • a continuous strip of steel having a thickness of substantially .011" which i is customarily used for making "crown" tin plate is provided in accordance with this invention with a tin coating having a weight of approximately one half to three quarters of a pound per base box.
  • the ingredients employed per gallon of water are sodium stannate-8 ounces; sodium acetate-3 ounces; caustic soda 1.6 ounces.- Sodium cyanide was included in the bath in an amount to assure that the electrodes corrode uniformly, for example, 3 ounces per gallon of water.
  • the current density was maintained at 16 amperes per square foot of cathode (strip) and the bath temperature was of the order of 175 F.
  • the metal was introduced to the bath at a temperature of about 125 to 160 F.
  • the coated metal as produced was formed into a roll 2i.
  • the rolls of the mill 2! through which the strip is now continuously fed are adjusted to exert a pressure of the order of 500,000 lbs, and at the bight of the rolls the pressure exerted per linear inch transversely of the strip upon the coated metal is about 17,000 lbs.
  • the speed of travel of the strip is 1200 feet per minute.
  • the coating is smooth and continuous and has the measure of rust resistance and in the present case rust resistance is substantially higher than with a comparable weight of hot-dip tin plate.
  • the product is diflicult to scratch indicating a desirable hardness and is readily worked without cracking and without peeling or I flaking of the tin coat.
  • the product I permanently retains decorative and protective this manner, the critical conditionsof cold-rollso ahighlustre. Continuityofthetincoatdmotes m coatings much better than conventional tin plate.
  • the strip instead of collecting the coated plate in a roll 2
  • the invention may be applied in connection with any suitable gauge of base metal and any appropriate weight of tin coating and while the metal is preferably fed as a continuous strip, the product may be formed in sheets of any desired length.
  • the method of making tin plate which comprises electrolytically coating tin on iron strip and cold rolling the coated metal with rolls rotating at uniform speed and under a pressure of from 250,000 pounds to 500,000 pounds to elongate the metal at least inch for any linear 25 inches in a single pass through the rolling instrmnentality and to impart a smooth, lustrous surface to the electroplated strip.

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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 Methods And Accessories (AREA)
  • Coating With Molten Metal (AREA)

Description

Sept. 4, 1945. Q GLOCK 2,384,086
' METHOD OF MAKING TIN FLA-TE Filed Dec. 22, 1939 karieszf 6206i uct more abrasion Patented Sept. 4, 1945 Charles-E. Glock, Baltim Crown Cork & Seal ore, Md., assignor to mpany,
Inc., Baltimore,
Md., a corporation of New York Application December 22, 1930, Serial No. 310,650
3 Claims.
This invention is an improved tin plate and I method for preparing'same.
One object of the invention is to provide tin plate with a tin coating having enhanced rust resistance.
Another object of the invention is to provide tin plate with a surface of increased hardness. The hardness characteristic renders the prodresistant and materially lessens the likelihood of scratching and incipient oxidation of the base.
A further object of the invention is to produce tin plate having a higher lustre and smoothness as compared with tin plate heretofore available. Since tin plate is employed frequently because it is desired to give a nice appearance to an article, the presence of a surface having an lmproved polish is very desirable.
An additional object of the invention is to produce tin plate having an increased affinity for lithograph and printing inks as well as decorative and protective lacquers and paints. Such coatings, as well known, are frequently applied to tin boxes, cans, container closures and other marked distinction to hot-dip tin plate which lraeggise of the presence of oily residue frequently e s a coa mg or allows the rubbed on same to be readily Another object of the invention is to provide tin plate having enhanced temper and workability. That is to say, the tin plate of this invention can be fabricated, as by stamping, drawing or other metal working operations into various shapes without danger of the metal cracklng or of the tin coating peeling or flaking from the metal base.
,3 Of equal importance with the foregoing, it is an obJect of the invention to provide a method which is simple and economical in operation. This method embodies a combination of steps comprising (1) electrolytically coating the base metal with tin followed by (2) a skin pass treatment in the nature of a high presure cold-rolling.
- Not only is an improved product obtained by this substantially uniform in thickness, and has increased adherence to the base metal, as evidenced by the ability of the tin plate to. resist peeling and flaking when subjected to severe metal working operations.
An additional object of the invention is to provide a method wherein continuous base metal strip or sheets of increased width, as compared to sheets platable by methods heretofore available, may be tin plated with facility. I have found that base metal having a width of 30 inches or more may be readily plated by the method of the present .invention. purposes, ability to increase the width of the tin plate affords a substantial economy, as in the manufacture of container closures and containers.
I havefound that in order to obtain a coating having the required brightness and other characteristics, it is necessary to control critically the pressure or the resulting elongation or reduction of the metal in the first pass through the mill in the cold-rolling operation. In other words,'I have found that successive passes will not produce the desired characteristics if a minimum elongation or reduction is not obtained in the first pass. For example, in reducing by cold-rolling, I have found that the first pass should produce an elongation of the order of at least inches for each 25 linear inches. Although I have found no objectionable maximum elongation, it is observed that very satisfactory results have been obtained when elongation varies from to 5% inches for each 25 linear inches.
Stated in terms of reduction in gauge, I find that the reduction in the first pass should be at least of one percent, which may be increased as desired. So far as the brightness of the coating is concerned, I have found no objectionable maximum reduction below which the reduction must be maintained in the first pass. However, it is desirable that the reductionnot reach a point where the strip is objectionably deformed as indicated by bowing or wrinkling. Consequently, the percentage of reduction in the first pass should be maintained below that which will cause such strip deformation. Subsequent passes do not destroy the effects obtained in the appearance of the metal when the elongation or reduction in the first pass is controlled in this manner. Stated in terms of pressure, I have found that the rolls of the mill should be adjusted to apply a pressure of'the order of from at least 250,000 to 500,000 lbs. Such a range of For many finish and coincident reduction when rolling, for example, a strip 30 inches wide and having a gauge of approximately .011 inch. This pressure may be determined inthe conventional way, by an instrument employed to register the elongation of the mill housing during the application of pressure. Suchinstruments are well known and are employed on substantially all types of rolling mills. The particular figures given were taken from such instrument applied to a 4-high Mesta tempering mill. When so controlled, the elongation and gauge reduction is of the order above recited. The metal may be fed through the mill at a rate of from 1200 to 2000 feet per minute.
.11; is, of course, well known that tin plate is relatively expensive because of the cost of the tin. With this invention, it has been found that smooth, nice-appearing coatings affording the desired protection of the base metal for certain uses such as for dry packages can be produced with as little as 1 5 pound of tin per base box. By base box, I mean the. area represented by -112 sheets of size 14 by 20 inches, i. e., substantially 33,000 square inches. Of course, coatings of increased weight may be applied with equal emciency; and the method lends itself to-regulation of 'the weight as desired. As is well known, by the hot-dip method, it is not ordinarily possible to reduce the weight of the coating below 1 /3 pounds per base box.
Economy in manufacture is important since tin plate is employed universally and particularly in the manufacture of numerous articles which must be sold at a very modest price.
For a more complete understanding of the invention reference is had to the accompanying drawing wherein Y Figure 1 is a diagrammatic illustration of the electro-coating operation;
Figure 2 is 'a diagrammatic illustration of the cold-rolling step; and
Figure 3 is a diagrammatic view showing the manner in which'the electro-coated band is continued to the cold-rolling instrumentality.
In practicing the invention, the customary steel or black iron of appropriate gauge is utilized. The metal is usually annealed and is supplied in continuous strips in the form of rolls by the steel mill,
, 1, is mounted upon a conventional uncoiler for feeding the strip continuously to the electrolytic coating apparatus. The numeral ll indicates an apparatus for welding ends of the strips together and the numeral l2 indicates a table having a holding clamp to maintain one end of the strip during the welding operation. The numeral l3 indicates the acid pickling tank which generally contains hydrofluoric or other suitable acid while the numeral N indicates a cold water rinsing tank. The strip I just prior to entering the electrolytic both I5 is heated by means of steam jets I6 to a temperature of about 160 F. The wiping rolls I! are of the character to permit a film of water to remain on the strip substantially until it enters the bath, whereby the strip is protected against the efiects of oxidation by the air and is introduced to the bath at a temperature to promote optimum coating and without substantially reducing the temperature of the bath. As will be understood, the heating means employed, namely, steam application is of a character which will not dry the surface of the strip; ,there is suflicient condensation of the steam to maintain 2,884,086 7 the desired protective moist film. The strip is fed through the'bath at varying speeds which may be as high as 500 feet a minute or greater. It will be noted that in the bath the strip is coated while traveling in vertically disposed position. The chemical reagents employed are preferably sodium stannate 5.4 ounces to 13 ounces; sodium acetate 2 ounces to 5 ounces; and caustic soda 1 ounce to 3 ounces, per-gallon of water. In some cases, sodium cyanide is included in the bath in an amount to insure that the electrodes corrode uniformly, for example, about 1 ounce to 6 ounces, per gallon of water.
The current density is maintained between 10 and '75 amperes per square foot of cathode (strip) and the temperature of the bath is. generally substantially between 158 to 200 F. As will be understood, the weight of the coating may be controlled by varying the time to which the strip is subjected to the bath as by regulating the speed of travel of the strip or by varying the amperage or by doing both.
From the bath, the coated strip is led through a cold water rinsing tank l8 and then through a hot water rinsing tank 19 whereupon it travels through a tensioning mechanism 20 and is wound into coils 2i. The coated metal is dull and soft and will have a thickness or weight of tin coat controlled in accordance with the use to be made of the tin plate.
The coils of coated metal are each transferred to a suitable uncoiler for continuously'feeding the strip to the cold-rolling instrumentality which is in the form of a usual a-ihigh mill as shown'at 22 in Figure 2. In this mill, the coated sheet is given a skin, pass treatment by means of a high pressure cold-rolling to impart thev properties of rust resistance, smoothness, hardness, temper and workability, and high lustre in a manner appreciably better than present available tin plate now possesses. The apparatus disclosed has the rolls rotating at uniform speed.
I have discovered that cold-rolling of tin coated metal, and particularly metal which has been electrolytically coated with tin, very substantially contributes to producing the aforesaid improved properties of. the'tin plate. That is to say, as above explained, I have found that in order to obtain a .coating having the required brightness 'and other improved characteristics, it is necessary to control critically (1) the pressure or (2) the resulting elongation or (3) the reduction of the metal in the first pass through the mill in the cold-rolling operation. It willbe observed that the skin pass treatment is decidedly rapid, and since the metal is fed as a continuous strip and only a single skin pass treatment is required a substantial economy is efiected in addition to stantially higher than tin plate of the same weight which has not been cold-rolled.
Moreover, the improved polish or high lustre of the tin plate is appreciable and 'very materially enhances the appearance of the product.
Since the principal purpose of coating steel with tin is to (1) protect the metal; and (2) beautify the same, it will be understood that both of these characteristics are substantially improved by the present invention.
By way of example, a continuous strip of steel having a thickness of substantially .011" which i is customarily used for making "crown" tin plate is provided in accordance with this invention with a tin coating having a weight of approximately one half to three quarters of a pound per base box. The ingredients employed per gallon of water are sodium stannate-8 ounces; sodium acetate-3 ounces; caustic soda 1.6 ounces.- Sodium cyanide was included in the bath in an amount to assure that the electrodes corrode uniformly, for example, 3 ounces per gallon of water. The current density was maintained at 16 amperes per square foot of cathode (strip) and the bath temperature was of the order of 175 F. The metal was introduced to the bath at a temperature of about 125 to 160 F.
The coated metal as produced was formed into a roll 2i. The rolls of the mill 2! through which the strip is now continuously fed are adjusted to exert a pressure of the order of 500,000 lbs, and at the bight of the rolls the pressure exerted per linear inch transversely of the strip upon the coated metal is about 17,000 lbs. The speed of travel of the strip is 1200 feet per minute. In
having a uniform coating which completely covera the metal base. Of particular importance, the coating is smooth and continuous and has the measure of rust resistance and in the present case rust resistance is substantially higher than with a comparable weight of hot-dip tin plate. The product is diflicult to scratch indicating a desirable hardness and is readily worked without cracking and without peeling or I flaking of the tin coat. Likewise, the product I permanently retains decorative and protective this manner, the critical conditionsof cold-rollso ahighlustre. Continuityofthetincoatdmotes m coatings much better than conventional tin plate.
From the foregoing, it will be appreciated that the combination of electrolytic coating and high pressure cold-rolling produces a very satisfactory product and affords a rapid and economical method.
In some cases, instead of collecting the coated plate in a roll 2|, the strip may be continued so as to be passed directly to the cold-rolling mill 22 as showninFigure 3.
'In connection with the electro-plating operation, it is sometimes desirable to give the band a cold-rolling treatment before it enters the bath, i. e., before the acid pickling, in order to properly temper the strip.
The invention may be applied in connection with any suitable gauge of base metal and any appropriate weight of tin coating and while the metal is preferably fed as a continuous strip, the product may be formed in sheets of any desired length.
I claim:
l. The method of making tin plate which comprises electrolytically coating tin on iron strip and cold rolling the coated metal with rolls rotating at uniform speed and under a pressure of from 250,000 pounds to 500,000 pounds to elongate the metal at least inch for any linear 25 inches in a single pass through the rolling instrmnentality and to impart a smooth, lustrous surface to the electroplated strip.
2. The method according to claim 1 wherein the coated metal is traveled between the rolls at a speedo! substantially 1,200 to 2,000 feet per minute. a
3. The method according to claim 1 which comprises exerting a roll pressure of 500,000 pounds and-a pressure at the bight of the rolls of about 17,000 pounds per linear inch transv'ersely of the strip.
CHARLES E. GLOCK.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2580801A (en) * 1946-04-10 1952-01-01 American Steel & Wire Co Method of making lustrous steel music wire
US2735788A (en) * 1956-02-21 Immersion tinning from stannate
US2854732A (en) * 1952-03-11 1958-10-07 British Iron Steel Research Process for the production of metals
US3200629A (en) * 1961-07-18 1965-08-17 Bethlehem Steel Corp Obtaining improved surface finishes on double reduced material
US3214820A (en) * 1963-02-08 1965-11-02 Nat Steel Corp Steel foil and manufacture
EP0562418A1 (en) * 1992-03-23 1993-09-29 Nkk Corporation Method for manufacturing tin-electroplated cold-rolled steel strip

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2735788A (en) * 1956-02-21 Immersion tinning from stannate
US2580801A (en) * 1946-04-10 1952-01-01 American Steel & Wire Co Method of making lustrous steel music wire
US2854732A (en) * 1952-03-11 1958-10-07 British Iron Steel Research Process for the production of metals
US3200629A (en) * 1961-07-18 1965-08-17 Bethlehem Steel Corp Obtaining improved surface finishes on double reduced material
US3214820A (en) * 1963-02-08 1965-11-02 Nat Steel Corp Steel foil and manufacture
EP0562418A1 (en) * 1992-03-23 1993-09-29 Nkk Corporation Method for manufacturing tin-electroplated cold-rolled steel strip
US5275716A (en) * 1992-03-23 1994-01-04 Nkk Corporation Method for manufacturing tin-electroplated cold-rolled steel strip

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