US3799750A - Can stock with differential protective coatings - Google Patents
Can stock with differential protective coatings Download PDFInfo
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- US3799750A US3799750A US00303888A US30388872A US3799750A US 3799750 A US3799750 A US 3799750A US 00303888 A US00303888 A US 00303888A US 30388872 A US30388872 A US 30388872A US 3799750 A US3799750 A US 3799750A
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- United States
- Prior art keywords
- per square
- square foot
- tinplate
- differential
- chromium
- 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
- 239000011253 protective coating Substances 0.000 title description 5
- 239000005028 tinplate Substances 0.000 abstract description 40
- 238000000576 coating method Methods 0.000 abstract description 31
- 239000011248 coating agent Substances 0.000 abstract description 24
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 abstract description 18
- 229910000423 chromium oxide Inorganic materials 0.000 abstract description 18
- 239000011651 chromium Substances 0.000 abstract description 17
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 abstract description 16
- 229910052804 chromium Inorganic materials 0.000 abstract description 16
- 238000000034 method Methods 0.000 abstract description 16
- JHWIEAWILPSRMU-UHFFFAOYSA-N 2-methyl-3-pyrimidin-4-ylpropanoic acid Chemical compound OC(=O)C(C)CC1=CC=NC=N1 JHWIEAWILPSRMU-UHFFFAOYSA-N 0.000 abstract description 6
- 238000005868 electrolysis reaction Methods 0.000 abstract description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 23
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 9
- 238000010186 staining Methods 0.000 description 9
- 230000002411 adverse Effects 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 238000005476 soldering Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 238000009924 canning Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- QDOXWKRWXJOMAK-UHFFFAOYSA-N dichromium trioxide Chemical compound O=[Cr]O[Cr]=O QDOXWKRWXJOMAK-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000004534 enameling Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/38—Chromatising
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S428/00—Stock material or miscellaneous articles
- Y10S428/922—Static electricity metal bleed-off metallic stock
- Y10S428/923—Physical dimension
- Y10S428/924—Composite
- Y10S428/926—Thickness of individual layer specified
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12535—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.] with additional, spatially distinct nonmetal component
- Y10T428/12542—More than one such component
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12535—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.] with additional, spatially distinct nonmetal component
- Y10T428/12611—Oxide-containing component
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12708—Sn-base component
- Y10T428/12722—Next to Group VIII metal-base component
Definitions
- differential tinplate having a trivalent chromium oxide coating thereon to the extent that about 1.00 to 1.50 mg. of chromium per square foot is provided on the heavily tinned side and about 0.40 to 0.80 mg. chromium per square foot is provided on the reverse lightly tinned side.
- the process involves the cathodic electrolysis of the differential tinplate in a dilute sodium-dichromate solution having a pH of from 3.5 to 5.5 at a temperature within the range 160 to 200 F.
- the heavily tinned side thereof is subjected to an electrical current of 100 to 170 coulombs per square foot while the reverse .side is subjected to not more than 45 coluombs per square foot, at current densities within the range to 170 amperes per square foot.
- US. patent application Ser. No. 14,283, filed Feb. 26, 1970 discloses a process for treating tinplate which provide exceptional resistance to oxidation, sulfide staining, detinning and abrasion.
- the process comprises an electrolytic treatment whereby the tinplate strip is made cathodic in a dilute sodium-dichromate solution thereby depositing a trivalent chromium oxide, such as chromic sesquioxide, Cr O -xH O, which provides a suitable protective coating normally providing from 1.0 to 1.5 mg. chromium per square foot.
- the coating provides exceptional resistance to sulfide staining and detinning, and further provides good adherence properties for lacquer, and resistance to oxide growth during storage.
- the crux of that inventive process resides in the application of a large quantity of electricity at reasonably high temperatures, i.e., 100 to 170 coulombs per square foot at 160 to 200 F.
- the protective chromium oxide coating does indeed provide the alleged beneficial results when applied to conventional tinplate grades solid commercially, i.e., those having tin coatings of at least about 0.50 pounds of tin per base box. This is equal to an individual tin surface of about 0.00115 pounds of tin per square foot.
- a chromium oxide coating is applied over tin coatings of less than 0.00115 pounds of tin per square foot (i.e., less than 0.50 pounds per base box)
- the solderability thereof is adversely affected.
- the chromium oxide coating so adversely affects the solderability thereof that the such can stock cannot be satisfactorily soldered by the jet soldering machines used by the can making industry.
- differential tinplate refers to tinplate stock having a heavier tin coating on one side thereof as compared to the other.
- differential tinplate is commonly used by the can making industry to provide a can with a heavy tin coating on the inside, and a lighter tin coating on the outside where corrosive environments are less severe.
- differential tinplate is sold with various combinations of different tin coatings thereon. The most common however are those having a lightly tinned side of 0.000575 pounds of tin per square foot of surface area, Le, a coating comparable to 0.25 pounds per base box.
- differential tinplate namely those grades having a lightly tinned side of less than 0.00115 pounds of tin per square foot of surface
- chromium oxide to enhance its resistance to oxidation, sulfide staining and detinning and at the same time maintain good solderability of the lightly tinned side if a differential chromium oxide coating is provided.
- the chromium oxide coating on the heavily tinned side should of course substantially be that provided by the process taught in patent application Ser. No. 14,233, i.e., normally from 1.0 to 1.5 mg. chromium per square foot of surface.
- the lightly tinned side should have a chromium oxide coating no greater than sufficient to provide from 0.4 to 0.8 mg. chromuim per square foot of surface, which can be assured by providing a quantity of electricity of no more than about 45 coulombs per square foot of surface.
- the coating weight 135 would have a tin coating of 0.00311 pounds of tin per square foot of surface.
- these grades of differential tinplate are known to frequently possess somewhat inferior soldering characteristics, especially when baked, as for example, after enameling.
- solderability is further adversely affected to the point where can makers can no longer get acceptable soldered joints.
- the crux of this invention resides in our discovery that the solderability of the lighter tin coated side of differential tinplate is not adversely affected, even when baked, if a like trivalent chromium oxide coating is electrolytically deposited thereon providing only from 0.40 to 0.80 mg. chromium per square foot of surface. Since the heavier tin coated side normally had good solderability not affected by the amount of chromium oxide coating, this side may then be given a more extensive protective coating,
- the process as taught in patent application Ser. No. 14,283 is applied. That is to say, the tinplate is immersed into a dilute sodium-dichromate solution having a pH of from 3.5 to 5.5 at a temperature within the range 160 to 200 F.
- the tinplate is made cathode adjacent to a conductive anode on the heavily tinned side of the tinplate, and sufiicient electrical current is applied to effect from 100 to 170 coulombs per square foot of tinplate surface.
- the applied current density does not appear to 'be critical since any current density within the range normally obtainable with commercial equipment will be effective.
- the desired chromium oxide coating a various current densities between and 170 amperes per square foot of surface.
- the total quantity of electrical current applied to that side directly should be no greater than 45 coulombs per square foot. Since it is preferred that both sides be treated simultaneously, the treating time for both sides will be the same. Therefore, it is necessary to merely utilize a correspondingly lower current density on the lightly tinned side of the tinplate sufficient to effect no more than 45 coulombs per square foot. It will be noted that there is no minimum value given for the coulombs applied to the lightly tinned side of the tinplate. Hence, any value between zero and 45 coulombs per square foot is sufficient.
- the desired product can be made Without any current directly applied to the lightly tinned side of the tinplate.
- the current applied to the heavily tinned side is so heavy at 100 to 170 coulombs per square foot that there is sufficient wrap-around current to deposit the minimum 0.4 mg. chromium per square foot on the lightly tinned side, even without a current directly applied thereto.
- the current density for the lightly tinned side of the tinplate may therefore be varied from 0 to 200 amperes per square foot.
- the strip was then rinsed in water and given the usual finishing treatment, i.e., drying, oiling and coiling.
- the differential applied current was effected by providing a larger anode surface area for the heavy current side.
- the strip was advanced through two separate tanks. In the first tank, the strip was passed adjacent to two S-foot anodes, both on the heavily tinned side of the strip. In the second tank, three anodes were used, two again on the heavily tinned side of the strip, and one on the lightly tinned side.
- the resulting sheet had 1.25 mg. chromium per square foot on the heavier tinned side and 0.80 mg. chromium per square foot on the other side.
- Can stock out from the strip was enameled and baked in accordance with usual canning procedures and easily soldered with jet soldering units.
- the salt concentration of the sodium-dichromate solution may be varied between 20 and 30 grams per liter, while the pH value may vary between 3.5 and 5.5 but is preferably maintained at 4.0 to 4.2.
- the temperature of the solution should be within the range to 200 F. or ideally at from 180 to F.
- the total current applied to that side should be within the broad range of 100 to 170 coulombs per square foot, or preferably 125 to 150 coulombs per square foot, yielding from 1.00 to 1.50 mg.
- the total current applied to that side should be maintained at no more than 45 coulombs per square foot, yielding 0.40 to 0.80 mg. of chromium per square foot.
- a differential tinplate having exceptional resistance to oxidation, sulfide staining and detinning and good solderability comprising a conventional differential tinplate having a coating of more than 0.00115 pound of tin per square foot on the heavily tinned side and from 0.000575 to 0.00115 pound of tin per square foot on the lightly tinned side, said differential tinplate having a differential trivalent chromium oxide coating thereon sufficient to provide from 1.00 to 1.50 mg. of chromium per square foot on the heavily tinned side and from 0.40 to 0.80 mg. of chromium per square foot on the lightly tinned side.
- a differential tinplate according to claim 1 in which the lightly tinned side thereof has a coating of about 0.000575 pound of tin per square foot.
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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)
Abstract
DIFFERENTIALLY TREATED DIFFERENTIAL TINPLATE HAVING A TRIVALENT CHROMIUM OXIDE COATING THEREON TO THE EXTENT THAT ABOUT 1.00 TO 1.50 MG. OF CHROMIUM PER SQUARE FOOT IS PROVIDED ON THE HEAVILY TINNED SIDE AND ABOUT 0.40 TO 0.80 MG. CHROMIUM PER SQUARE FOOT IS PROVIDED ON THE REVERSE LIGHTLY TINNED SIDE. THE PROCESS INVOLVES THE CATHODIC ELECTROLYSIS OF THE DIFFERENTIAL TINPLATE IN A DILUTE SODIUM-DICHROMATE SOLUTION HAVING A PH OF FROM 3.5 TO 5.5 AT A TEMPERATURE WITHIN THE RANGE 160 TO 200*F. THE HEAVILY TINNED SIDE THEREOF IS SUBJECTED TO AN ELECTRICAL CURRENT OF 100 TO 170 COULOMBS PER SQUARE FOOT WHILE THE REVERSE SIDE IS SUBJECTED TO NOT MORE THAN 45 COLUOMBS PER SQUARE FOOT, AT CURRENT DENSITIES WITHIN THE RANGE 10 TO 170 AMPERES PER SQUARE FOOT.
Description
United States Patent O 3,799,750 CAN STOCK WITH DIFFERENTIAL PROTECTIVE COATINGS James E. Bird, Franklin Township, Westmoreland County, and Paul R. Carter, Monroeville, Pa., assignors to United States Steel Corporation No Drawing. Application Aug. 27, 1971, Ser. No. 17 5,728, now Patent No. 3,7 49,651, dated July 31, 1973, which is a continuation-in-part of abandoned application Ser. No. 840,519, July 9, 1969. Divided and this application Nov. 6, 1972, Ser. No. 303,888
Int. Cl. B32b 15/04 US. Cl. 29-495 T 2 Claims ABSTRACT OF THE DISCLOSURE Differentially treated differential tinplate having a trivalent chromium oxide coating thereon to the extent that about 1.00 to 1.50 mg. of chromium per square foot is provided on the heavily tinned side and about 0.40 to 0.80 mg. chromium per square foot is provided on the reverse lightly tinned side. The process involves the cathodic electrolysis of the differential tinplate in a dilute sodium-dichromate solution having a pH of from 3.5 to 5.5 at a temperature within the range 160 to 200 F. The heavily tinned side thereof is subjected to an electrical current of 100 to 170 coulombs per square foot while the reverse .side is subjected to not more than 45 coluombs per square foot, at current densities within the range to 170 amperes per square foot.
This is a division, of application Ser. No. 175,728, filed Aug. 27, 1971 now Pat. 3,749,651, dated July 31, 1973, which was a continuation-in-part of Ser. No. 840,519, filed July 9, 1969, now abandoned.
BACKGROUND OF THE INVENTION There are many known processes for treating tinplate to further enhance its corrosion resistance characteristics. Of particular concern are processes which inhibit corrosion of particularly corrosive foods, such as sulfur bearing food products which cause sulfide staining, or other corrosive foods wrich may cause detinning.
US. patent application Ser. No. 14,283, filed Feb. 26, 1970, discloses a process for treating tinplate which provide exceptional resistance to oxidation, sulfide staining, detinning and abrasion. The process comprises an electrolytic treatment whereby the tinplate strip is made cathodic in a dilute sodium-dichromate solution thereby depositing a trivalent chromium oxide, such as chromic sesquioxide, Cr O -xH O, which provides a suitable protective coating normally providing from 1.0 to 1.5 mg. chromium per square foot. The coating provides exceptional resistance to sulfide staining and detinning, and further provides good adherence properties for lacquer, and resistance to oxide growth during storage. The crux of that inventive process resides in the application of a large quantity of electricity at reasonably high temperatures, i.e., 100 to 170 coulombs per square foot at 160 to 200 F.
In practicing the above inventive process, we have learned that the protective chromium oxide coating does indeed provide the alleged beneficial results when applied to conventional tinplate grades solid commercially, i.e., those having tin coatings of at least about 0.50 pounds of tin per base box. This is equal to an individual tin surface of about 0.00115 pounds of tin per square foot. When such a chromium oxide coating is applied over tin coatings of less than 0.00115 pounds of tin per square foot (i.e., less than 0.50 pounds per base box), the solderability thereof is adversely affected. In fact, the chromium oxide coating so adversely affects the solderability thereof that the such can stock cannot be satisfactorily soldered by the jet soldering machines used by the can making industry.
Although corrosion resistant tinplate is seldom. sold with coatings lighter than 0.00115 pounds of tin per square foot of surface area, i.e., less than 0.50 pounds per base box, such coatings are quite common on one surface of differential tinplate. Differential tinplate as used herein, refers to tinplate stock having a heavier tin coating on one side thereof as compared to the other. For economic reasons, differential tinplate is commonly used by the can making industry to provide a can with a heavy tin coating on the inside, and a lighter tin coating on the outside where corrosive environments are less severe..Differential tinplate is sold with various combinations of different tin coatings thereon. The most common however are those having a lightly tinned side of 0.000575 pounds of tin per square foot of surface area, Le, a coating comparable to 0.25 pounds per base box.
It follows, therefore, that although the process of patent application Ser. No. 14,283 is perfectly suitable for conventional tinplate, it is not suitable for differential tinplate having tin coatings on the. lightly tinned side of less than 0.00115 pounds of tin per square foot of surface. When the process is applied to such differential tinplate, the solderability of the lightly tinned side is so adversely affected that can manufacturers cannot produce an acceptable solder thereon.
SUMMARY OF THE INVENTION This invention is predicated upon our discovery that differential tinplate, namely those grades having a lightly tinned side of less than 0.00115 pounds of tin per square foot of surface, can be suitably coated with chromium oxide to enhance its resistance to oxidation, sulfide staining and detinning and at the same time maintain good solderability of the lightly tinned side if a differential chromium oxide coating is provided. The chromium oxide coating on the heavily tinned side should of course substantially be that provided by the process taught in patent application Ser. No. 14,233, i.e., normally from 1.0 to 1.5 mg. chromium per square foot of surface. The lightly tinned side, however, should have a chromium oxide coating no greater than sufficient to provide from 0.4 to 0.8 mg. chromuim per square foot of surface, which can be assured by providing a quantity of electricity of no more than about 45 coulombs per square foot of surface.
It is therefore an object of this invention to provide a differentially treated differential tinplate having exceptional resistance to sulfide staining and detinning and at the same time maintain good solderability.
It is another object of this invention to provide a process for treating differential tinplate to provide a heavy chromium oxide coating on the heavily tinned side of the tinplate, thereby enhancing resistance to oxidation, sulfide staining and detinning, and to provide a lighter chromium oxide coating on the reverse side to maintain good solderability of the tinplate.
DESCRIPTION OF THE PREFERRED EMBODIMENT Although this invention could be applied to any differential tinplate, it is mostly beneficial to those grades wherein the heavily tinned side exceeds 0.00115 pounds of tin per square foot of surface, i.e., 0.50 pounds per base box, and the lightly tinned side contains less than that amount down to about 0.000575 pounds per square foot of surface. Concerning commercial grades therefore, this invention is most advantageously applied to the commercial grades 50*25, -25, -25 and -25. (The coating weight 135 would have a tin coating of 0.00311 pounds of tin per square foot of surface.) Even without chromium oxide coatings, these grades of differential tinplate are known to frequently possess somewhat inferior soldering characteristics, especially when baked, as for example, after enameling. As noted above, when such differential tinplate is provided with a chromium oxide coating as described in patent application Ser. No. 14,283, the solderability is further adversely affected to the point where can makers can no longer get acceptable soldered joints.
The crux of this invention resides in our discovery that the solderability of the lighter tin coated side of differential tinplate is not adversely affected, even when baked, if a like trivalent chromium oxide coating is electrolytically deposited thereon providing only from 0.40 to 0.80 mg. chromium per square foot of surface. Since the heavier tin coated side normally had good solderability not affected by the amount of chromium oxide coating, this side may then be given a more extensive protective coating,
e.g., normally in excess of 1 mg. chromium per square foot to provide suitable resistance to oxidation, sulfide staining and detinning. For the heavily tinned side therefore, the process as taught in patent application Ser. No. 14,283 is applied. That is to say, the tinplate is immersed into a dilute sodium-dichromate solution having a pH of from 3.5 to 5.5 at a temperature within the range 160 to 200 F. The tinplate is made cathode adjacent to a conductive anode on the heavily tinned side of the tinplate, and sufiicient electrical current is applied to effect from 100 to 170 coulombs per square foot of tinplate surface. The applied current density does not appear to 'be critical since any current density within the range normally obtainable with commercial equipment will be effective. Specifically we have produced the desired chromium oxide coating a various current densities between and 170 amperes per square foot of surface.
To assure that only 0.4 to 0.8 mg. chromium per square foot is applied to the lightly tinned side of the tinplate, the total quantity of electrical current applied to that side directly should be no greater than 45 coulombs per square foot. Since it is preferred that both sides be treated simultaneously, the treating time for both sides will be the same. Therefore, it is necessary to merely utilize a correspondingly lower current density on the lightly tinned side of the tinplate sufficient to effect no more than 45 coulombs per square foot. It will be noted that there is no minimum value given for the coulombs applied to the lightly tinned side of the tinplate. Hence, any value between zero and 45 coulombs per square foot is sufficient. Indeed, the desired product can be made Without any current directly applied to the lightly tinned side of the tinplate. This is because the current applied to the heavily tinned side is so heavy at 100 to 170 coulombs per square foot that there is sufficient wrap-around current to deposit the minimum 0.4 mg. chromium per square foot on the lightly tinned side, even without a current directly applied thereto. The current density for the lightly tinned side of the tinplate may therefore be varied from 0 to 200 amperes per square foot.
As a specific example of the process of this invention, we have passed 100-25 differential tinplate strip through a sodium-dichromate solution containing to grams of the salt per liter, while maintaining the solution at a pH of about 4.0 and a temperature of about 190 F. During the passage, the strip was connected as cathode in an electrolyzing circuit to a suitable current source. Conductive anodes of mild steel were disposed about 1 /2 inches from each face of the strip. The heavily tinned side of the strip was subjected to an electrical current of coulombs per square foot while the lighter tinned sidewas subjected to 40 coulombs per square foot. The strip was then rinsed in water and given the usual finishing treatment, i.e., drying, oiling and coiling. The differential applied current was effected by providing a larger anode surface area for the heavy current side. Specifically, the strip was advanced through two separate tanks. In the first tank, the strip was passed adjacent to two S-foot anodes, both on the heavily tinned side of the strip. In the second tank, three anodes were used, two again on the heavily tinned side of the strip, and one on the lightly tinned side. The resulting sheet had 1.25 mg. chromium per square foot on the heavier tinned side and 0.80 mg. chromium per square foot on the other side. Can stock out from the strip was enameled and baked in accordance with usual canning procedures and easily soldered with jet soldering units.
Although the above described specific example did utilize the optimum process parameters, these parameters may be varied somewhat depending upon personal preferances and economics. Specifically, the salt concentration of the sodium-dichromate solution may be varied between 20 and 30 grams per liter, while the pH value may vary between 3.5 and 5.5 but is preferably maintained at 4.0 to 4.2. The temperature of the solution should be within the range to 200 F. or ideally at from 180 to F. In order to provide a good heavy protective coating on the heavily coated side which will be resistant to sulfide staining and detinning, the total current applied to that side should be within the broad range of 100 to 170 coulombs per square foot, or preferably 125 to 150 coulombs per square foot, yielding from 1.00 to 1.50 mg. of chromium per square foot. In order to enhance solderability of the lightly tinned side, however, the total current applied to that side should be maintained at no more than 45 coulombs per square foot, yielding 0.40 to 0.80 mg. of chromium per square foot.
We claim:
1. A differential tinplate having exceptional resistance to oxidation, sulfide staining and detinning and good solderability comprising a conventional differential tinplate having a coating of more than 0.00115 pound of tin per square foot on the heavily tinned side and from 0.000575 to 0.00115 pound of tin per square foot on the lightly tinned side, said differential tinplate having a differential trivalent chromium oxide coating thereon sufficient to provide from 1.00 to 1.50 mg. of chromium per square foot on the heavily tinned side and from 0.40 to 0.80 mg. of chromium per square foot on the lightly tinned side.
2. A differential tinplate according to claim 1 in which the lightly tinned side thereof has a coating of about 0.000575 pound of tin per square foot.
References Cited UNITED STATES PATENTS 2,327,127 8/1943 Rath 29-195 T X 2,780,592 2/1957 Wick et al 29-195 T X 3,160,481 12/1964 Shoemaker 29195 T 3,479,162 11/1969 Yanabu et a1 29-195 T 3,491,001 1/ 1970 Shackleford et al. 20456 R 3,526,486 9/1970 Smith et al 29-195 T X L. DEWAYNE RUTLEDGE, Primary Examiner E. L. WEISE, Assistant Examiner
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US00303888A US3799750A (en) | 1972-11-06 | 1972-11-06 | Can stock with differential protective coatings |
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US00303888A US3799750A (en) | 1972-11-06 | 1972-11-06 | Can stock with differential protective coatings |
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US3799750A true US3799750A (en) | 1974-03-26 |
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US00303888A Expired - Lifetime US3799750A (en) | 1972-11-06 | 1972-11-06 | Can stock with differential protective coatings |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362056A1 (en) * | 1976-08-18 | 1978-03-17 | Toyo Kohan Co Ltd | STEEL SHEET USEFUL FOR FORMING CANS OF FOOD AND BEVERAGE |
FR2362943A1 (en) * | 1976-08-25 | 1978-03-24 | Toyo Kohan Co Ltd | STEEL SHEET FOR DRINK AND FOOD CANS |
FR2385818A1 (en) * | 1977-04-01 | 1978-10-27 | Cockerill | Steel sheet with very thin protective tin coating - obtd. by electroplating; and then heating to form a tin-iron alloy |
EP0063933A1 (en) * | 1981-04-23 | 1982-11-03 | Nippon Steel Corporation | Steel strip having differentiated multilayer coatings and being useful for manufacture of cans |
US4446156A (en) * | 1978-02-23 | 1984-05-01 | The Broken Hill Proprietary Company Limited | Manufacture of tinplate and tinplate containers |
US4863060A (en) * | 1986-04-29 | 1989-09-05 | Weirton Steel Corporation | Flat-rolled steel can stock product |
US5094924A (en) * | 1988-10-19 | 1992-03-10 | Kenzo Matsui | Polyester resin film laminated steel sheet for drawn and ironed can |
US20040134912A1 (en) * | 2000-07-18 | 2004-07-15 | Tarulis George J | Drawn wall ironed can for light colored fruits |
-
1972
- 1972-11-06 US US00303888A patent/US3799750A/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362056A1 (en) * | 1976-08-18 | 1978-03-17 | Toyo Kohan Co Ltd | STEEL SHEET USEFUL FOR FORMING CANS OF FOOD AND BEVERAGE |
FR2362943A1 (en) * | 1976-08-25 | 1978-03-24 | Toyo Kohan Co Ltd | STEEL SHEET FOR DRINK AND FOOD CANS |
FR2385818A1 (en) * | 1977-04-01 | 1978-10-27 | Cockerill | Steel sheet with very thin protective tin coating - obtd. by electroplating; and then heating to form a tin-iron alloy |
US4446156A (en) * | 1978-02-23 | 1984-05-01 | The Broken Hill Proprietary Company Limited | Manufacture of tinplate and tinplate containers |
US4483907A (en) * | 1978-02-23 | 1984-11-20 | The Broken Hill Proprietary Company Limited | Manufacture of tinplate and tinplate containers |
US4508480A (en) * | 1978-02-23 | 1985-04-02 | The Broken Hill Proprietary Company Limited | Manufacture of tinplate and tinplate containers |
EP0063933A1 (en) * | 1981-04-23 | 1982-11-03 | Nippon Steel Corporation | Steel strip having differentiated multilayer coatings and being useful for manufacture of cans |
US4442181A (en) * | 1981-04-23 | 1984-04-10 | Nippon Steel Corporation | Steel strip having differentiated multilayer coatings and being useful for manufacturing of cans |
US4863060A (en) * | 1986-04-29 | 1989-09-05 | Weirton Steel Corporation | Flat-rolled steel can stock product |
US5094924A (en) * | 1988-10-19 | 1992-03-10 | Kenzo Matsui | Polyester resin film laminated steel sheet for drawn and ironed can |
US20040134912A1 (en) * | 2000-07-18 | 2004-07-15 | Tarulis George J | Drawn wall ironed can for light colored fruits |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: USX CORPORATION, A CORP. OF DE, STATELESS Free format text: MERGER;ASSIGNOR:UNITED STATES STEEL CORPORATION (MERGED INTO);REEL/FRAME:005060/0960 Effective date: 19880112 |