JPH08158092A - Production of granular tin plated steel plate - Google Patents

Abstract

PURPOSE: To efficiently produce a granular tin plated steel sheet at a low cost by greatly increasing the upper limit of current density at the time of depositing a granular tin. CONSTITUTION: Electrolyic treatment is enabled at the high current density by executing tin plating in a plating bath using phenol sulfonic acid as a base material and a steel sheet is electrolyzed at the current density of 10-50A/dm<2> in the plating bath containing >20g/l to 50g/l bivalent tin ion and 5-30g/l phenol sulfonic acid expressed in terms of sulfuric acid to execute tin plating to the surface of the steel sheet by 0.02-2.8g/m<2> coating weight. To attain more excellent coating material adhesivity, the surface of the steel sheet is subjected to tin plating by 0.3-1.0g/m<2> coating weight by electrolyzing it at the current density of 10-35A/dm<2> .

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a material for a welding can suitable for filling and storing foods, beverages, etc., and is generally a granular tin-plated steel sheet used as a material for a can after being subjected to chromate treatment or the like. Of the manufacturing method of.

[0002]

2. Description of the Related Art Welding cans occupy a large proportion in the field of beverage cans and food cans, and it can be said that the reduction of material costs is an important industrial issue. By the way, as materials for beverage cans and food cans, tin plate, LTS (tinted tin plate), T
FS (Tin Free Steel) and the like have been widely used from the past, and recently, these materials are often used as an organic coating by coating or laminating a resin film. Comparing the suitability of LTS and TFS as materials for a welding can, TFS has the characteristics of excellent cost and coating adhesion and film adhesion, but has the disadvantage of extremely poor weldability. On the other hand, LTS has excellent weldability, but it has a T value in terms of cost and paint adhesion.
Inferior to FS.

In the past, various attempts have been made to compensate for the disadvantages of LTS and TFS. For example, JP-A-62-103390 and JP-A-62-149897.
The publication discloses a surface-treated steel plate for a welding can in which tin is scattered in an island shape by performing reflow treatment after tin plating. This surface-treated steel sheet is intended to reduce the amount of tin deposited by scattering tin in an island shape to reduce the cost, and to improve the adhesion of the paint while ensuring the weldability. However, since such a tin-plated steel sheet is manufactured through a reflow process, part of the plated tin inevitably alloys with the base iron. Since metal tin mainly contributes to the weldability, the above tin-plated steel sheet inevitably requires a large amount of tin plating as compared with the one not subjected to the reflow process.

On the other hand, in JP-A-2-298277 and JP-A-2-310378, a surface-treated steel sheet in which granular tin is deposited on the steel sheet surface by using a sulfuric acid plating bath without using a reflow process. Has been proposed. Also, Japanese Patent Publication No. 6-33506 proposes a method for producing a surface-treated steel sheet in which granular tin is deposited using an acidic tin plating bath containing no brightening agent.

[0005]

However, in these production methods, the upper limit of the current density at which granular tin is deposited is 15 A / dm.
^As low as ² . Therefore, a long electrolysis time is required to obtain a desired tin plating deposition amount, the number of passes and the number of electrolytic baths inevitably increase, and economical and efficient granular tin plating cannot be performed. Therefore, an object of the present invention is to provide a method capable of significantly increasing the upper limit of the current density when precipitating granular tin, whereby a granular tin-plated steel sheet can be efficiently manufactured at low cost. It is in.

[0006]

In the production method of the present invention for solving the above problems, tin plating is carried out in a plating bath based on phenol sulfonic acid (PSA), whereby electrolysis at a high current density is performed. The processing is made possible, and the characteristic configuration is as follows. (1) 10 A / d of a steel sheet in a plating bath containing 20 g / l or more and 50 g / l or less of divalent tin ions and 5 g / l or more and 30 g / l or less of phenolsulfonic acid in terms of sulfuric acid.
Granular tin-plated steel sheet characterized by being electrolyzed at a current density of m ² or more and 50 A / dm ² or less, and applying tin plating with a deposition amount of 0.02 g / m ² or more and 2.8 g / m ² or less to the steel sheet surface. Manufacturing method.

(2) Steel plate exceeds 20 g / l and exceeds 50 g / l
The following divalent tin ions and 5 g / l or more and 30 g in terms of sulfuric acid
In a plating bath containing 1 / l or less of phenolsulfonic acid, electrolytic treatment is performed at a current density of 10 A / dm ² or more and 35 A / dm ² or less, and the amount of deposition on the steel plate surface is 0.3 g / m ² or more 1.
A method for producing a granular tin-plated steel sheet, which comprises performing tin plating at 0 g / m ² or less.

[0008]

The details and reasons for limitation of the present invention will be described below. In the present invention, in a phenol sulfonic acid-based plating bath containing 20 g / l or more and 50 g / l or less of divalent tin ions and 5 g / l or more and 30 g / l or less of phenol sulfonic acid in terms of sulfuric acid, a steel sheet is used as a cathode. As described above, tin plating is applied, and by using such a plating bath, electrolytic treatment at high current density becomes possible. When the concentration of divalent tin ions in the plating bath is 20 g / l or less, the precipitation of tin becomes an abnormal precipitation morphology called dendrite, so that the electrolysis efficiency is remarkably inferior and the weldability is also inferior. On the other hand, if the divalent tin ion concentration exceeds 50 g / l, sludge is significantly generated, which is not preferable.

If the concentration of phenolsulfonic acid is less than 5 g / l in terms of sulfuric acid, the tin particles become dendrites, resulting in poor electrodeposition and electrolysis efficiency and poor weldability. On the other hand, 30
If it exceeds g / l, electrolysis efficiency is lowered due to gas generation.
In such a phenol sulfonic acid type plating bath, the steel plate (usually degreased and pickled steel plate) is used in an amount of 10 to 5
Electrolyzed at a current density of 0 A / dm ² and deposited amount 0.02
~ 2.8 g / m ² tin plating is applied. According to the present invention, the desired granular tin plating can be obtained even when the electrolytic treatment is performed at a current density extremely higher than that of the conventional method.

If the current density is less than 10 A / dm ² , the electrolysis time becomes too long, and the efficient electrolysis treatment in a short time, which is the aim of the present invention, cannot be realized. On the other hand, when the current density exceeds 50 A / dm ² , tin is in a dendrite-precipitated form, so that the electrolysis efficiency is remarkably inferior, and the electrodeposition of tin is hindered by the generation of gas, which deteriorates the weldability.
On the other hand, if the amount of deposited tin plating is less than 0.02 g / m ² , the amount of metallic tin remaining after coating baking or film lamination cannot be sufficiently secured, resulting in poor weldability. On the other hand, when the amount of deposited tin plating exceeds 2.8 g / m ² , the effect of improving the weldability due to the increased amount of tin is almost saturated, and the material cost associated with tin plating increases, which is not preferable.

When a tin-plated steel sheet is used as a material for a welding can, its weldability depends on the amount of metallic tin. Since the reflow process is not performed in the manufacturing method of the present invention, all the tin adhering at the time of manufacturing the steel sheet is metallic tin. However, when manufacturing a welded can from a product steel sheet that has been subjected to chromate treatment, etc. on a tin-plated steel sheet, the alloying of tin and base metal progresses to some extent due to the baking treatment performed before welding and the heat treatment during film lamination. It is inevitable. Therefore, in order to ensure weldability, it is necessary to leave a sufficient amount of metallic tin even after coating baking or film laminating to ensure weldability. The amount of adhesion is an important factor. From the viewpoint of leaving metallic tin, tin alloying progresses in the thickness direction of the tin layer, so if the tin deposition amount is the same, the tin layer is formed in a granular form rather than being formed uniformly. It is more advantageous, and even with the same granular tin, granular tin in the shape of a mountain is more advantageous than flat granular tin. On the other hand, in terms of coating adhesion and laminate adhesion, the base iron treated with chromate or the like is superior to the base tin treated with chromate or the like.

Therefore, in the form in which tin plating is formed in a granular form on the surface of the steel sheet as in the present invention, the weldability is ensured at the granular tin part and the paint adhesion and the laminate adhesion are ensured at the base iron part. You can In order to satisfy both the weldability and the paint adhesion / lamination adhesion as described above, the average particle diameter of the granular tin is 0.01 to 10 μm, and the formation density of the granular tin is 0.1 to 100 μm ^2. Although it is preferable to set the number to about 200, according to the manufacturing conditions of the present invention described above, the granular tin in such a form can be easily obtained.

The granular tin formed on the surface of the steel sheet does not have sufficient weldability if the average particle size and the forming density are less than the above lower limits, while the average particle size and the forming density are above the upper limit. If the value is exceeded, the paint adhesion and laminate adhesion will be poor. Here, in order to further improve the paint adhesion and the laminate adhesion, the average particle size of the granular tin is 0.5 to 5 μm,
The formation density of the granular tin is preferably 0.4 to 40 per 100 μm ^{2, and} for this purpose, electrolytic treatment is performed in the plating bath at a current density of 10 to 35 A / dm ² , and the amount of the deposited tin is 0. It is preferable to apply tin plating of ^{3 to} 1.0 g / m ² .

In the present invention, since electrolytic treatment is carried out in a plating bath based on phenolsulfonic acid, the upper limit of the current density can be set to 50 A / dm ^2, and the conventional method using a sulfuric acid-based plating bath (current density Upper limit of: 15 A / dm ² )
The operating conditions are dramatically improved compared to. For example, a granular tin-plated steel sheet having a tin deposition amount of 0.55 g / m ^{2 and} a striping speed of 4
When manufacturing at 00m / min, it is about 4m according to the conventional method.
Electrode length is required. On the other hand, according to the method of the present invention, an electrode length of 1.2 m is sufficient by performing electrolytic treatment at a current density of 50 A / dm ² , and the required electrode length can be greatly shortened as compared with the conventional method. If this is considered for vertical tin plating lines, for example, it is possible to improve in each vertical tank,
Assuming that each electrode length of down is 1 m, at least 4 passes of the electrode are required in the conventional method, and therefore at least 3 tanks including the dipping tank immediately before plating are required as the tank. On the other hand, in the method of the present invention, two passes of the electrode are sufficient, and therefore, two tanks are sufficient, including the one for immersion immediately before plating.

Therefore, when carrying out the method of the present invention using a normal vertical tin plating line (electrode length: about 1 m),
By performing the electrolytic treatment at a current density of 30 A / dm ² or more, the electrolytic treatment can be performed in two passes, which is extremely advantageous in terms of equipment. In other words, according to the method of the present invention, the desired granular tin plating can be performed in a remarkably shorter electrolysis time than the conventional method, and therefore, assuming the same equipment as the conventional method, the line speed is remarkably high. And high productivity can be obtained.

[0016]

[Examples] A low carbon cold-rolled steel sheet having a plate thickness of 0.22 mm, which was cold-rolled, continuously annealed and temper-rolled by a conventional method, was degreased and pickled, and then subjected to the following plating bath based on phenolsulfonic acid. Tin plating was performed under the conditions using the steel sheet as a cathode to produce granular tin-plated steel sheets having different particle sizes, densities, and amounts of deposits of granular tin. Chromium plating or chromate treatment is applied to these granular tin-plated steel sheets under the following conditions to obtain metallic chromium of 100 mg / m ² and chromium of 10
Surface-treated steel sheets coated with mg / m ² of chromium oxide were manufactured, and the weldability and paint adhesion of these surface-treated steel sheets were examined. The results are shown in Tables 1 and 2 together with the specific conditions of tin plating, the form of granular tin and the amount of deposition.

Regarding the average particle size of the granular tin, the surface of the steel sheet after tin plating was observed by SEM, and the diameter of the granular tin was measured at randomly specified locations. The average value was determined and this was used as the average particle size. The formation density of granular tin was also observed by SEM,
The number of granular tin particles per 10 μm ^{2 at} 5 randomly specified points was counted, and the average value of the number of granular tin particles at these 5 points was determined, and this was taken as the formation density of granular tin particles.

Tin Plating Conditions (A) Bath Conditions Tin Ion Concentration 10 to 50 g / l Phenolsulfonic Acid Concentration (Sulfuric Acid Conversion) 3 to 40 g / l (B) Electrolysis Treatment Conditions Current Density 10 to 60 A / dm ² Electrolysis Time 0. 01-4.5 sec

Chromium plating conditions (A) Bath conditions Chromium oxide concentration 100 g / l Sulfuric acid concentration 1.2 g / l Bath temperature 50 ° C. (B) Electrolysis treatment conditions Current density 50 A / dm ² Electrolysis time 1 sec

Chromate treatment condition (A) Bath condition Chromium oxide concentration 50 g / l Sulfuric acid concentration 0.1 g / l Bath temperature 50 ° C. (B) Electrolysis treatment condition Current density 10 A / dm ² Electrolysis time 1 sec

(1) Evaluation of Weldability The surface-treated steel sheet was heat-treated at 210 ° C. for 30 minutes, and then a sample of 50 mm square was cut out. Two pieces of this sample were overlapped and sandwiched between electrodes having an electrode diameter of 4.5 mmφ, and the electrodes were welded at an electrode pressure of 50 kgf and a welding current of 1 A. The contact resistance at that time was measured and evaluated by the following. ◯: Contact resistance is 500 μΩ or less, good weldability ×: Contact resistance is more than 500 μΩ, poor weldability

(2) Evaluation of paint adhesion The epoxy phenolic paint was baked on the test material (coating adhesion amount: 50 mg / m ² baking condition: 205 ° C x 10 minutes), and then 105 ° C x in an aqueous solution. A retort treatment was performed for 60 minutes, and then a scratch was made with a scoring needle to perform a tape peeling test on the coating film. ⊚: Does not peel at all. ◯: Some peeling is observed near the scratch. X: Peeling occurs.

In Tables 1 and 2, Examples 1 to 6 of the present invention are examples in which the divalent tin Sn ion concentration was changed within the range of the present invention. Comparative Example 1 is an example in which the divalent tin Sn ion concentration is less than the lower limit value of the present invention, and the electrolysis efficiency is extremely poor and the weldability is also poor. Inventive Example 7 to Inventive Example 10 are examples in which the PSA concentration was changed within the range of the present invention. Comparative Examples 2 and 3 are Examples in which the PSA concentration is out of the range of the present invention, and both have extremely poor electrolysis efficiency and poor weldability.

Inventive Examples 11 to 15 are Examples in which the current density was changed within the scope of the present invention. Comparative Example 4 is an example in which the current density exceeds the upper limit value of the present invention, the electrolysis efficiency is poor, and the weldability is also poor. Inventive Example 16 to Inventive Example 25 are examples in which the amount of tin plating deposited was changed within the range of the present invention. Comparative Example 5 is an example in which the amount of deposited tin plating is less than the lower limit value of the present invention, and the weldability is poor. Inventive Example 17 to Inventive Example 21 are examples corresponding to claim 2 of the present application, and all have particularly excellent paint adhesion.

[0025]

[Table 1]

[0026]

[Table 2]

[0027]

According to the present invention described above, tin plating can be carried out at a significantly higher current density than the conventional method for producing a granular tin-plated steel sheet, so that the required electrode length can be reduced as compared with the conventional method. It can be significantly shortened, and tin plating can be performed with a small number of tanks. Therefore, it is also possible to perform the desired granular tin plating in a significantly shorter electrolysis time than the conventional method, and when the same equipment as the conventional method is used,
The line speed can be remarkably increased as compared with the conventional method, and the granular tin-plated steel sheet can be manufactured with high productivity and at low cost. Further, since the phenol sulfonic acid bath used in the present invention is cheaper than other organic acid baths, the granular tin-plated steel sheet can be manufactured at that low cost.
In addition, since it is possible to operate with a small number of tanks, when using the conventional plating treatment equipment, it is possible to divert part of the plating treatment section to another, which is more expensive than the conventional method. Can be significantly reduced. Further, there is an advantage that it is easy to switch to another type on the same plating line.

Claims (2)

[Claims] 1. A steel sheet containing more than 20 g / l and 50 g / l or less of divalent tin ions and 5 g / l or more and 30 g / l in terms of sulfuric acid.
in a plating bath containing 1 or less phenolsulfonic acid,
Electrolytic treatment was performed at a current density of 10 A / dm ² or more and 50 A / dm ² or less, and the amount of adhesion on the steel plate surface was 0.02 g / m ² or more and 2.8.
A method for producing a granular tin-plated steel sheet, which comprises applying tin plating of g / m ² or less. 2. A steel sheet containing divalent tin ions of more than 20 g / l and 50 g / l or less and 5 g / l or more and 30 g / l in terms of sulfuric acid.
in a plating bath containing 1 or less phenolsulfonic acid,
Electrolyzed at a current density of 10 A / dm ² or more and 35 A / dm ² or less, and the amount of deposition on the steel plate surface is 0.3 g / m ² or more and 1.0 g
A method for producing a granular tin-plated steel sheet, which comprises performing tin plating at a rate of not more than 1 m ² / m ² .