Technical Field
[0001] The present invention relates to a method for manufacturing a steel sheet coated
with a zinc-based coating layer having a reaction layer.
Background Art
[0002] A steel sheet coated with a zinc-based coating layer has been used in a wide range
of applications mainly in automobile bodies, domestic electrical appliances, and building
materials. There is a known technique in which properties such as press formability,
corrosion resistance, and surface appearance quality of a steel sheet coated with
a zinc-based coating layer used in such applications are improved by forming a reaction
layer on the surface of the steel sheet.
[0003] However, conventionally, a steel sheet coated with a zinc-based coating layer before
a reaction layer is formed thereon has an unnecessary layer having a thickness of
less than 10 nm composed of oxides of, for example, Zn and Al, which are impurity
chemical elements, in the outermost surface layer thereof. Since such an unnecessary
oxide layer decreases the reactivity of a chemical conversion treatment such as a
zinc phosphate treatment or a chromate treatment, it is necessary to set a long reaction
time in order to form a sufficient amount of the reaction layer.
[0004] An increase in reaction time is accompanied by an increase in equipment cost, line
length, and running cost for, for example, electricity and gas.
[0005] In response to such a problem, there is a known technique in which a reaction time
is decreased by bringing the surface layer of a steel sheet coated with a zinc-based
coating layer into contact with an alkaline aqueous solution in order to remove an
unnecessary oxide layer existing on the surface layer of the steel sheet before a
reaction layer is formed.
[0006] Patent Literature 1 describes a technique in which a galvanized steel sheet is treated
by using a SiO
2-containing chromate solution after the steel sheet has been brought into contact
with an alkaline aqueous solution.
[0007] Also, there is a known technique in which an oxide film is intentionally formed after
a treatment has been performed by using an alkaline aqueous solution.
[0008] Patent Literature 2 and Patent Literature 3 describe techniques in which an oxide
layer is formed after the surface of a galvanized steel sheet has been brought into
contact with an alkaline aqueous solution.
[0009] Patent Literature 4 describes a technique in which an oxide layer is formed after
the surface of a galvannealed steel sheet has been brought into contact with an alkaline
aqueous solution.
[0010] Patent Literature 5 describes a technique in which an oxide layer containing a crystal-structured
substance expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O is formed after the surface of a galvanized steel sheet has been brought into contact
with an alkaline aqueous solution.
Citation List
Patent Literature
[0011]
PTL 1: Japanese Unexamined Patent Application Publication No. 5-279868
PTL 2: Japanese Unexamined Patent Application Publication No. 2006-183074
PTL 3: Japanese Unexamined Patent Application Publication No. 2006-233280
PTL 4: Japanese Unexamined Patent Application Publication No. 2005-97741
PTL 5: Japanese Patent Application No. 2015-530230
Summary of Invention
Technical Problem
[0012] In the case of the techniques according to Patent Literature 1 through Patent Literature
5, it is possible to decrease the reaction time required to form a reaction layer
through contact with an alkaline aqueous solution. However, in the case of ordinarily
used continuous treatment equipment, since pressing flaws occur on the surface of
a steel sheet due to precipitates of Zn and Al generated in the alkaline aqueous solution
adhering to deflecting rolls and supporting rolls, there is a case where problems
related to surface appearance such as an irregularity in surface appearance occurs
after a reaction layer has been formed.
[0013] The present invention has been completed in view of the situation described above.
An object of the present invention is to provide a method for manufacturing a steel
sheet coated with a zinc-based coating layer in which it is possible to remove an
unnecessary oxide layer on the surface of the zinc-based coating layer through contact
with an alkaline aqueous solution and in which it is possible to prevent a problem
related to surface appearance due to precipitates generated in an alkaline aqueous
solution. Solution to Problem
[0014] The present inventors diligently conducted investigations in order to solve the problems
described above, and, as a result, found that it is possible to solve the problems
described above by adding a specific chelating agent to an alkaline aqueous solution
which is used before a reaction layer is formed, resulting in the completion of the
present invention. More specifically, the present invention provides the following.
[0015] The method for manufacturing a steel sheet coated with a zinc-based coating layer
of the first invention in order to solve the problems described above is a method
for manufacturing a steel sheet coated with a zinc-based coating layer having a reaction
layer on the surface of the steel sheet, the method including:
bringing a steel sheet coated with a zinc-based coating layer into contact for 1.0
second or more with an alkaline aqueous solution containing one or more chelating
agents selected from among sodium gluconate, sodium glucoheptonate, sodium citrate,
tartaric acid, arabonic acid, galactonic acid, sorbit, mannite, glycerin, EDTA, and
sodium tripolyphosphate in a total amount of 0.050 mass% or more and having a pH of
10.0 or more as a pre-treatment before a formation of the reaction layer, and
forming the reaction layer being an oxide layer containing a crystal-structured substance
expressed by Zn4(SO4)1-x(CO3)x(OH)6·nH2O,.
[0016] The method for manufacturing a steel sheet coated with a zinc-based coating layer
of the second invention in order to solve the problems described above is the method
for manufacturing a steel sheet coated with a zinc-based coating layer according to
the first invention, wherein pH of the alkaline aqueous solution is 12.6 or more.
Advantageous Effects of Invention
[0017] According to the present invention, it is possible to effectively remove oxides on
the surface of a zinc-based coating layer through contact with an alkaline aqueous
solution. In addition, in an alkaline treatment which is performed in order to decrease
the time required to form a reaction layer, since it is possible to decrease the amount
of, for example, precipitates of Al and Zn, it is possible to obtain a steel sheet
coated with a zinc-based coating layer having a reaction layer and having good surface
appearance.
Brief Description of Drawing
[0018] [Fig. 1] Fig. 1 is a schematic diagram illustrating evaluation criteria for an irregularity
in surface appearance.
Description of Embodiments
[0019] Hereafter, the embodiments of the present invention will be described. Here, the
present invention is not limited to the embodiments described below. In the present
invention, the term "a steel sheet coated with a zinc-based coating layer" refers
to a steel sheet having a coating film containing mainly zinc on the surface thereof
regardless of its manufacturing method, and the meaning of the term includes a zinc-coated
steel sheet, a zinc-alloy-coated steel sheet, a steel sheet coated with a coating
layer containing particles dispersed in zinc, and so forth. That is, the meaning of
the term "a zinc-based coating layer" includes a zinc coating layer, a zinc-alloy
coating layer, a coating layer containing particles dispersed in zinc, and so forth.
[0020] The present invention is a method for manufacturing a steel sheet coated with a zinc-based
coating layer, the steel sheet having a reaction layer, that is, an oxide layer containing
a crystal-structured substance expressed by Zn
4(SO
4)1-x(CO
3)
x(OH)
6·nH
2O, with which it is possible to effectively remove an unnecessary oxide layer existing
on the surface of the zinc-based coating layer. The present invention includes, for
example, a process in which zinc-based coating is performed, a process in which the
steel sheet is brought into contact with an alkaline aqueous solution, and a process
in which an oxide layer containing a crystal-structured substance expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O is formed. Hereafter, each of the processes will be described.
[0021] Process in which zinc-based coating is performed
[0022] First, a process in which zinc-based coating is performed will be described. In the
process in which zinc-based coating is performed, there is no particular limitation
on the method used for forming a zinc-based coating layer, and a commonly used method
such as a galvanizing method or an electro-galvanizing method may be used. In addition,
there is no particular limitation on the conditions used for performing an electro-galvanizing
treatment or a galvanizing treatment, and preferable conditions may be used appropriately.
Here, in the case where galvanizing is performed, it is preferable that Al be added
to the galvanizing bath from the viewpoint of a countermeasure against dross. In this
case, there is no particular limitation on constituent chemical elements other than
Al. That is, even in the case where Pb, Sb, Si, Sn, Mg, Mn, Ni, Ti, Li, Cu, and the
like are contained in addition to Al, there is no decrease in the effects of the present
invention.
[0023] Here, there is no particular limitation on the grade of steel sheet on which zinc
coating is performed, and a steel sheet of any steel grade such as low-carbon steel,
ultralow-carbon steel, IF steel, or a high-strength steel sheet, in which various
alloy chemical elements are added, may be used. In addition, the steel sheet may be
any of a hot-rolled steel sheet and a cold-rolled steel sheet. There is no particular
limitation on the thickness of the steel sheet. Here, it is preferable that the thickness
be 0.4 mm to 5.0 mm from the viewpoint of applications such as automobile bodies,
domestic electrical appliances, and building materials.
[0024] Moreover, in a process in which zinc-based coating is performed, after a galvanizing
treatment is performed, a galvannealed steel sheet may be manufactured by performing
an alloying treatment. In the present invention, there is no particular limitation
on the conditions for performing an alloying treatment, and preferable conditions
may be used appropriately.
[0025] Process in which a steel sheet is brought into contact with an alkaline aqueous solution
[0026] After zinc-based coating has been performed, a contact treatment is performed by
using an alkaline aqueous solution. The alkaline aqueous solution which is used in
this contact treatment has a pH of 10.0 or more. In the case where the pH is less
than 10.0, an insufficient amount of oxide layer is removed. It is preferable that
the pH be 12.6 or more, because it is possible to effectively decrease the contact
time with the alkaline aqueous solution.
[0027] On the other hand, it is preferable that the pH be 14.0 or less from the viewpoint
of preventing the dissolution of the zinc-based coating layer and the blackening of
surface appearance.
[0028] Specific chelating agents are contained in the alkaline aqueous solution in a total
amount of 0.050 mass% or more. In the case where there is an increase in the amount
of, for example, precipitates of Al and Zn in the alkaline aqueous solution, the solution
has a suspension-like appearance. In the present invention, 0.050 mass% or more of
chelating agents are added to the alkaline aqueous solution in order to decrease the
amounts of, for example, the precipitates of Al and Zn.
[0029] The chelating agents described above are one or more selected from among sodium gluconate,
sodium glucoheptonate, sodium citrate, tartaric acid, arabonic acid, galactonic acid,
sorbit, mannite, glycerin, EDTA, and sodium tripolyphosphate. It is preferable to
use sodium gluconate as the chelating agent described above, because it is capable
of chelating Al and Zn and inexpensive.
[0030] In the case where the total content of chelating agents in the alkaline aqueous solution
is less than 0.050 mass%, there is an insufficient increase in the solubility of Al
and Zn in the alkaline aqueous solution. It is preferable that the content of chelating
agents in the alkaline aqueous solution be 0.100 mass% or more from the viewpoint
of decreasing the amount of precipitates in the alkaline aqueous solution. On the
other hand, it is preferable that the content of chelating agents in the alkaline
aqueous solution be 10.0 mass% or less from the viewpoint of chemical cost.
[0031] It is preferable that the temperature of the alkaline aqueous solution be in the
range of 20°C to 70°C, or more preferably 40°C to 70°C, in order to decrease the contact
time between the alkaline aqueous solution and a steel sheet.
[0032] There is no limitation on the kind of an alkaline builder. Here, it is preferable
to use a chemical such as NaOH from the viewpoint of cost. In order to achieve the
desired pH of the alkaline aqueous solution, the amount of the alkaline builder is
appropriately controlled. In addition, the alkaline aqueous solution may contain substances
and chemical components other than chemical elements such as Zn, Al, and Fe, which
are contained in a zinc-based coating solution.
[0033] There is no particular limitation on the method used for bringing the alkaline aqueous
solution into contact with a steel sheet coated with a zinc-based coating layer (in
particular, an oxide layer on the surface thereof), and examples of the method include
one in which the steel sheet coated with a zinc-based coating layer is dipped in the
alkaline aqueous solution and one in which the steel sheet coated with a zinc-based
coating layer is sprayed with the alkaline aqueous solution.
[0034] A time during which the steel sheet coated with a zinc-based coating layer is brought
into contact with the alkaline aqueous solution is 1.0 second or more. In the case
where the contact time is less than 1.0 second, since an insufficient amount of oxides
is removed from the surface of the zinc-based coating layer, there is an insufficient
decrease in reaction time during which a reaction layer is formed. It is preferable
that the time during which the steel sheet coated with a zinc-based coating layer
is brought into contact with the alkaline aqueous solution be 10.0 seconds or less
from the viewpoint of equipment cost and productivity.
[0035] In the present invention, a skin pass rolling may be performed after the process
in which zinc-based coating is performed and before or after the treatment is performed
by using an alkaline aqueous solution. There is an increase in reactivity in a portion
of a steel sheet which has been brought into contact with rolls for skin pass rolling,
because an unnecessary oxide layer of Al and Zn is removed from the surface of the
zinc-based coating layer through the contact with the rolls.
[0036] Process in which a reaction layer is formed
[0037] Usually, after the process in which a steel sheet is brought into contact with the
alkaline aqueous solution, and then rinsing with water and drying are performed, a
treatment is performed in order to form a reaction layer, that is, an oxide layer
containing a crystal-structured substance expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O.
[0038] In the present invention, the term "an oxide layer containing a crystal-structured
substance expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O" refers to the layer of a reaction product which is formed on the surface of a steel
sheet through a chemical reaction which occurs as a result of contact between a zinc-based
coating layer and a chemical treatment solution. An example of a treatment for forming
an oxide layer containing a crystal-structured substance expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O includes an oxide-layer-forming process in which a steel sheet coated with a zinc-based
coating layer is brought into contact with an acid solution containing sulfate ions,
then held for 1 second to 60 seconds, and then washed with water and a neutralizing
treatment process in which the surface of the oxide layer formed in the oxide-layer-forming
process described above is kept in contact with an alkaline aqueous solution for 0.5
seconds or more, then washed with water, and then dried. The alkaline aqueous solution
may contain P ions in an amount of 0.01 g/L or more in terms of P concentration and
carbonate ions in an amount of 0.1 g/L or more in terms of carbonate ion concentration.
The present invention is not limited to such a treatment method as long as a crystal-structured
substance expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O exists on the surface of a steel sheet.
EXAMPLE 1
[0039] Hereafter, the present invention will be described on the bases of examples. The
scope of the present invention is not limited to the examples described below.
[0040] A skin pass rolling was performed on steel sheets which had been prepared by performing
a galvanizing treatment on cold-rolled steel sheets having a thickness of 0.7 mm and
a width of 1100 mm. Subsequently, the steel sheets were subjected to a treatment for
removing an oxide layer in which the steel sheets were kept in contact with the alkaline
aqueous solutions prepared under the conditions given in Tables 1-1 and 1-2 over the
specified times, then washed with water, and then dried.
[0041] Also, steel sheets which had been prepared by performing a galvanizing treatment
followed by an alloying treatment and skin pass rolling on a cold-rolled steel sheets
having a thickness of 0.7 mm and a width of 1100 mm and steel sheets which had been
prepared by performing an electro-galvanizing treatment on cold-rolled steel sheets
having a thickness of 0.7 mm and a width of 1100 mm were kept in contact with the
alkaline aqueous solutions in the same procedures as those described above, then washed
with water, and then dried.
[0042] On the steel sheets coated with a zinc-based coating layer obtained as described
above, determination of the thickness of an unnecessary oxide layer on the surface
of the zinc-based coating layer after a treatment had been performed by using an alkaline
aqueous solution and evaluation of the irregularity in surface appearance after a
reaction layer had been formed were performed, and determination of suspended solids
(SS) contained in the alkaline aqueous solutions was performed. Here, the pH of the
alkaline aqueous solution was determined by using commercially available glass electrodes.
[0043] Subsequently, a treatment for forming an oxide layer containing a crystal-structured
substance expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O was performed by dipping the steel sheets in a sulfuric acid solution containing
30 g/L of sodium acetate trihydrate and having a pH of 1.5, then squeezing the steel
sheets by using rolls, and then holding the steel sheets for 10 seconds. Then, after
having performed washing with water, drying was performed. Subsequently, a neutralizing
treatment was performed by using a treatment solution containing 9.8 g/L of sodium
pyrophosphate and 0.48 g/L of sodium carbonate decahydrate.
(1) Determination of the thickness of an unnecessary oxide layer
[0044] After the contact with the alkaline aqueous solution, an X-ray fluorescence spectrometer
was used for determining the thickness of an unnecessary oxide layer formed on the
surface of the steel sheet coated with a zinc-based coating layer. It is judged that
a case where the thickness of the oxide layer (thickness of an oxide film) is 4 nm
or less as a case where there is a decrease in reaction time required to form a reaction
layer. It is judged that a case where the thickness of an oxide film is 2 nm or less
as a case where there is a further decrease in reaction time.
[0045] At the time of the determination, by setting the voltage and current of a tube to
be respectively 30 kV and 100 mA, and by setting a dispersive crystal to be TAP, an
O-Kα ray was detected. At the time of the determination of an O-Kα ray, intensity
was determined at a peak position and a background position in order to calculate
the net intensity of an O-Kα ray. Here, the integration time at each of the peak position
and the background position was 20 seconds.
[0046] In addition, silicon wafers which were cleaved into an appropriate size and whose
surface were respectively covered with silicon oxide films having a film thickness
of 96 nm, 54 nm, and 24 nm were set on the sample stage with these series of samples
so that it was possible to calculate the intensity of an O-Kα ray of each of such
silicon oxide films. A calibration curve is prepared to determine the relationship
between the thickness of an oxide layer and the intensity of an O-Kα ray by using
such data. The thickness of the oxide layer of the sample is calculated as the thickness
of the oxide layer in terms of the thickness of a silicon oxide film.
(2) Evaluation of the irregularity in surface appearance and determination of the
thickness of an oxide film after a surface oxidation treatment has been performed
[0047] After having performed a treatment for forming an oxide layer on the surface of each
of galvanized steel sheets, galvannealed steel sheets, and electro-galvanized steel
sheets which had been subjected to a contact treatment by using an alkaline aqueous
solution, an irregularity in surface appearance was evaluated by performing visual
observation and microscopic observation. That is, by preparing a solution containing
5.0 g/L of ferrous sulfate and 50 g/L of sodium acetate heptahydrate which was adjusted
so as to have a pH of 2.0 by using sulfuric acid, by applying the prepared treatment
solution to each of the various kinds of the coated steel sheets which had been subjected
to a contact treatment by using an alkaline aqueous solution so that the thickness
of the solution was 3 µm, by holding the coated steel sheet for 10 seconds, by then
washing the coated steel sheet with water, and by then drying the coated steel sheet,
a treatment for forming an oxide layer was performed. Here, the observation area was
70 mm × 150 mm. With reference to the surface appearance samples illustrated in Fig.
1, evaluation was performed on a scale of one to five. Grade 4 indicates a satisfactory
case, and grade 5 indicates a more satisfactory case.
(3) Determination of suspended solids (SS)
[0048] The alkaline aqueous solution which had been used for the treatment of 100 tons or
more of a steel sheet coated with a zinc-based coating layer was collected and subjected
to suction filtration by using a membrane filter having a pore size of 1 µm. After
having dried the material retained on the filter at a temperature of 110°C, the weight
of the dried material was determined, and the weight was expressed in units of mg/L.
The amount of production for which the determined value was more than 10 mg/L was
recorded. A case where the amount of steel sheets treated for which the determined
value was more than 10 mg/L was 3000 tons or more was judged as satisfactory from
the viewpoint of productivity. In addition, a case where the determined value was
not more than 10 mg/L even after 5000 tons of steel sheets had been treated was judged
as a case of no suspended solids (represented by "> 5000" in Tables 1-1 and 1-2).
In the case of Nos. 1, 54, and 56 where a treatment was not performed by using an
alkaline aqueous solution, such determination was not performed.
[0049] The results obtained as described above are given in Tables 1-1 and 1-2. Here, the
conditions on which the tests of No. 15 and No. 41 were performed were same, and the
conditions on which the tests of No. 20 and No. 28 were performed were same.
[Table 1-1]
| |
Contact Treatment Condition with Alkaline Treatment Solution |
Result |
| No. |
Material for Sample |
Alkaline Aqueous Solution |
Thickness of Oxide Film |
Irregularity in Surface Appearance |
Amount of Production for More than 10 mg of Suspended Solid Generated |
Note |
| Alkaline Builder |
Chelating Agent |
Temperature |
pH |
Contact Method |
Contact Time |
| Kind of Chemical |
Concentration (mass%) |
Kind of Chemical |
Concentration (mass%) |
°C |
|
|
second |
nm |
grade |
ton |
| 1 |
Galvanized Steel Sheet |
None |
- |
- |
- |
- |
- |
- |
- |
8 |
5 |
- |
Comparative Example |
| 2 |
Sodium Hydrate |
0.01 |
- |
- |
50 |
10.0 |
Dip |
3.0 |
3 |
1 |
500 |
Comparative Example |
| 3 |
|
0,5 |
- |
- |
|
12.6 |
|
|
2 |
1 |
200 |
Comparative Example |
| 4 |
|
Sodium Hydrate |
0.01 |
Sodium Gluconate |
0.005 |
50 |
10.0 |
Dip |
3.0 |
3 |
4 |
1500 |
Comparative Example |
| 5 |
|
|
|
|
0.050 |
|
|
|
|
3 |
5 |
>5000 |
Example |
| 6 |
|
|
|
|
0.100 |
|
|
|
|
3 |
5 |
>5000 |
Example |
| 7 |
|
|
|
|
0.500 |
|
|
|
|
3 |
5 |
>5000 |
Example |
| 8 |
|
|
|
|
1.0 |
|
|
|
|
3 |
5 |
>5000 |
Example |
| 9 |
|
|
|
|
2.0 |
|
|
|
|
3 |
5 |
>5000 |
Example |
| 10 |
|
|
|
|
3.0 |
|
|
|
|
3 |
5 |
>5000 |
Example |
| 11 |
|
Sodium Hydrate |
0.5 |
Sodium Gluconate |
0.005 |
50 |
12.6 |
Dip |
3.0 |
2 |
4 |
1500 |
Comparative Example |
| 12 |
|
|
|
|
0.050 |
|
|
|
|
2 |
5 |
>5000 |
Example |
| 13 |
|
|
|
|
0.100 |
|
|
|
|
2 |
5 |
>5000 |
Example |
| 14 |
|
|
|
|
0.500 |
|
|
|
|
2 |
5 |
>5000 |
Example |
| 15 |
|
|
|
|
1.0 |
|
|
|
|
2 |
5 |
>5000 |
Example |
| 16 |
|
|
|
|
2.0 |
|
|
|
|
2 |
5 |
>5000 |
Example |
| 17 |
|
|
|
|
3.0 |
|
|
|
|
2 |
5 |
>5000 |
Example |
| 18 |
|
|
|
|
10.0 |
|
|
|
|
2 |
5 |
>5000 |
Example |
| 19 |
|
Sodium Hydrate |
0.01 |
Sodium Gluconate |
1.0 |
50 |
10.0 |
Dip |
0.5 |
7 |
5 |
>5000 |
Comparative Example |
| 20 |
|
|
|
|
|
|
|
|
1.0 |
4 |
5 |
>5000 |
Example |
| 21 |
|
|
|
|
|
|
|
|
5.0 |
2 |
5 |
>5000 |
Example |
| 22 |
|
|
|
|
|
|
|
|
10.0 |
1 |
5 |
>5000 |
Example |
| 23 |
|
Sodium Hydrate |
0.5 |
Sodium Gluconate |
1.0 |
50 |
12.6 |
Dip |
0.5 |
6 |
5 |
>5000 |
Comparative Example |
| 24 |
|
|
|
|
|
|
|
|
1.0 |
2 |
5 |
>5000 |
Example |
| 25 |
|
|
|
|
|
|
|
|
5.0 |
1 |
5 |
>5000 |
Example |
| 26 |
|
|
|
|
|
|
|
|
10.0 |
0 |
5 |
>5000 |
Example |
| 27 |
|
Sodium Hydrate |
0.001 |
Sodium Gluconate |
1.0 |
50 |
9.0 |
Dip |
1.0 |
7 |
5 |
>5000 |
Comparative Example |
| 28 |
|
|
0.01 |
|
|
|
10.0 |
|
|
4 |
5 |
>5000 |
Example |
| 29 |
|
|
0.05 |
|
|
|
11.0 |
|
|
4 |
5 |
>5000 |
Example |
| 30 |
|
|
0.1 |
|
|
|
12.0 |
|
|
3 |
5 |
>5000 |
Example |
| 31 |
|
|
10 |
|
|
|
13.0 |
|
|
2 |
5 |
>5000 |
Example |
| 32 |
|
|
70 |
|
|
|
13.5 |
|
|
1 |
5 |
>5000 |
Example |
| 33 |
|
|
98 |
|
|
|
14.0 |
|
|
0 |
5 |
>5000 |
Example |
| 34 |
|
Sodium Hydrate |
0.001 |
Sodium Gluconate |
1.0 |
50 |
9.0 |
Dip |
3.0 |
7 |
5 |
>5000 |
Comparative Example |
| 35 |
|
|
0.05 |
|
|
|
11.0 |
|
|
3 |
5 |
>5000 |
Example |
| 36 |
|
|
0.1 |
|
|
|
12.0 |
|
|
3 |
5 |
>5000 |
Example |
| 37 |
|
|
10 |
|
|
|
13.0 |
|
|
2 |
5 |
>5000 |
Example |
| 38 |
|
|
70 |
|
|
|
13.5 |
|
|
1 |
5 |
>5000 |
Example |
| 39 |
|
|
98 |
|
|
|
14.0 |
|
|
0 |
5 |
>5000 |
Example |
[Table 1-2]
| |
Contact Treatment Condition with Alkaline Treatment Solution |
Result |
| No. |
Material for Sample |
Alkaline Aqueous Solution |
Thickness of Oxide Film |
Irregularity in Surface Appearance |
Amount of Production for More than 10 mg of Suspended Solid Generated |
Note |
| Alkaline Builder |
Chelating Agent |
Temperature |
pH |
Contact Method |
Contact Time |
| Kind of Chemical |
Concentration (mass%) |
Kind of Chemical |
Concentration (mass%) |
°C |
|
|
second |
nm |
grade |
ton |
| 40 |
|
Sodium Hydrate |
0.5 |
Sodium Gluconate |
1.0 |
20 |
12.6 |
Dip |
3.0 |
3 |
5 |
>5000 |
Example |
| 41 |
|
|
|
|
|
50 |
|
|
|
2 |
5 |
>5000 |
Example |
| 42 |
|
|
|
|
|
70 |
|
|
|
1 |
5 |
>5000 |
Example |
| 43 |
|
Sodium Hydrate |
0.5 |
Sodium Gluconate |
1.0 |
50 |
12.6 |
Spray |
3.0 |
2 |
5 |
>5000 |
Example |
| 44 |
|
Sodium Hydrate |
0.5 |
Sodium Glucoheptonate |
1.0 |
50 |
12.6 |
Dip |
3.0 |
2 |
5 |
>5000 |
Example |
| 45 |
|
|
|
Sodium Citrate |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 46 |
|
|
|
Tartaric Acid |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 47 |
|
|
|
Arabonic Acid |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 48 |
|
|
|
Galactonic Acid |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 49 |
|
|
|
Sorbit |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 50 |
|
|
|
Mannite |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 51 |
|
|
|
Glycerin |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 52 |
|
|
|
EDTA |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 53 |
|
|
|
Sodium Tripolyphosphate |
|
|
|
|
|
2 |
5 |
>5000 |
Example |
| 54 |
Galvannealed Steel Sheet |
None |
- |
- |
- |
- |
- |
- |
- |
10 |
5 |
- |
Comparative Example |
| 55 |
Sodium Hydrate |
0.5 |
Sodium Gluconate |
1.0 |
50 |
12.6 |
Dip |
3.0 |
2 |
5 |
>5000 |
Example |
| 56 |
Electro-galvanized Steel Sheet |
None |
- |
- |
- |
- |
|
- |
- |
7 |
5 |
- |
Comparative Example |
| 57 |
Sodium Hydrate |
0.5 |
Sodium Gluconate |
1.0 |
50 |
12.6 |
Dip |
3.0 |
1 |
5 |
>5000 |
Example |
[0050] From Tables 1-1 and 1-2, the following facts are clarified.
[0051] Surface analysis was performed on Nos. 1 through 57 after unnecessary oxide layer
had been removed by using an alkaline aqueous solution.
[0052] In the case of comparative examples Nos. 1, 54 and 56 where a contact treatment was
not performed by using an alkaline aqueous solution, the thickness of an oxide layer
was 7 nm to 10 nm, which means that insufficient amount of oxide layer was removed.
[0053] In the case of Nos. 2 and 3, although a contact treatment was performed by using
an alkaline aqueous solution, these cases are deficient examples (comparative example)
on the point that a chelating agent was not added to the alkaline aqueous solution.
It was possible to remove sufficient amount of oxide layer. However, since suspended
solids were generated in the alkaline aqueous solution as the amount of production
of steel sheets increased, there was a deterioration in surface appearance.
[0054] In the case of Nos. 4 and 11, although a contact treatment was performed by using
an alkaline aqueous solution containing a chelating agent, these cases are examples
of an insufficient concentration of chelating agent (comparative examples). It was
possible to remove sufficient amount of oxide layer. However, suspended solids were
generated in the alkaline aqueous solution as the amount of production of steel sheets
increased.
[0055] In the case of Nos. 19 and 23, although a contact treatment was performed by using
an alkaline aqueous solution containing a chelating agent, these cases are examples
of a short contact time (comparative examples). The thickness of an oxide layer was
6 nm to 7 nm, which means that insufficient amount of oxide layer was removed.
[0056] In the case of Nos. 27 and 34, although a contact treatment was performed by using
an alkaline aqueous solution containing a chelating agent, these cases are examples
of a low pH (comparative examples). The thickness of an oxide layer was 7 nm, which
means that insufficient amount of oxide layer was removed.
[0057] Nos. 24 and 28 through 33 are the examples of the present invention in which the
effect of pH was clarified by performing a contact treatment with a contact time of
1.0 second. In the case where pH was 12.6 or more, since it was possible to decrease
the thickness of an oxide film to 2 nm or less even with a contact time of 1.0 second,
it was possible to decrease a reaction time required to form a reaction layer to a
higher degree.
EXAMPLE 2
[0058] Analysis was performed on the oxide layer containing a crystal-structured substance
expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O of Nos. 2 through 53, 55, and 57.
(4) Confirmation of Zn4(SO4)1-x(CO3)x(OH)6·nH2O
[0059] By brushing the surface of the oxide layer containing a crystal-structured substance
expressed by Zn
4(SO
4)
1-x(CO
3)
x(OH)
6·nH
2O by using a stainless brush having bristles having a diameter of 0.15 mm and a length
of 45 mm and ethanol, and by suction filtering of the obtained ethanol solution, the
components of the film were taken in the form of powder. Quantitative analysis of
C was performed by programmed temperature gas chromatography on the components of
the film taken in the form of powder components by using a gas chromatography mass
spectrometer. A pyrolytic furnace was connected to the front part of the gas chromatography
mass spectrometer. By charging about 2 mg of the taken powder sample into the pyrolytic
furnace, and by transporting a gas generated in the pyrolytic furnace in which the
temperature was increased from 30°C to 500°C at an increasing rate of 5°C/min to the
gas chromatography mass spectrometer with helium, the composition of the gas was analyzed.
The column temperature at the time of GC/MS analysis was set to be 300°C.
Existence form of C
[0060] By using the components of the film taken in the form of powder by using the same
method as that described above, and by performing gas chromatography mass spectrometry,
the existence form of C was analyzed.
Existence forms of Zn, S, O, and H
[0061] By using an X-ray photoelectron spectrometer, the existence forms of S, Zn, and O
were analyzed. By using an Al-Ka monochrome radiation source, narrow measurement of
spectra corresponding to Zn-LMM and S-2p was performed.
Existence form of P
[0062] By using an X-ray-absorption fine-structure spectrometer, the existence form of P
was analyzed. By using beam line BL27A of Photon Factory, High Energy Accelerator
Research Organization, the observation of an X-ray absorption fine structure (ZAFS)
was performed at room temperature. By irradiating the surface of a degreased sample
with a monochrome radiation beam, the spectrum of an X-ray absorption near-edge structure
(XANES) of P-K shell was observed by using a total electron yield method (TEY) by
performing sample absorption current measurement.
Quantitative determination of crystallization water
[0063] By using a differential thermogravimetric analyzer, the amount of decrease in weight
at a temperature of 100°C or lower was determined. About 15 mg of powder sample was
used for the determination. After having charging the sample into the analyzer, by
increasing the temperature from room temperature (about 25°C) to 1000°C at an increasing
rate of 10°C/min, a change in weight while the temperature was being increased was
recorded.
Identification of crystal structure
[0064] By performing X-ray diffractometry on the components of the film taken in the form
of powder by using the same method as that described above, the crystal structure
was presumed. The determination was performed with Cu being used as the target under
the conditions of an acceleration voltage of 40 kV, a tube current of 50 mA, a scanning
speed of 4 deg/min, and a scanning range of 2° to 90°.
[0065] Hereafter, the obtained results regarding Nos. 2 through 38, 40 through 53, 55,
and 57 will be described.
[0066] From the results obtained by performing gas chromatography mass spectrometry, it
was clarified that, since CO
2 emission was observed in a temperature range of 150°C to 500°C, C existed in the
form of carbonates.
[0067] From the results of the analysis using an X-ray photoelectron spectrometer, it was
clarified that, since a peak corresponding to Zn-LMM was observed in the vicinity
of 987 eV, Zn existed in the form of zinc hydroxide. Similarly, it was clarified that,
since a peak corresponding to S-2p was observed in the vicinity of 171 eV, S existed
in the form of sulfates.
[0068] From the results of the analysis using an X-ray-absorption fine-structure spectrometer,
it was clarified that, since peaks were observed in the vicinity of each of 2153 eV,
2158 eV, and 2170 eV, P existed in the form of pyrophosphates.
[0069] From the results of the analysis using a differential thermogravimetric analyzer,
it was clarified that, since a decrease in weight by 11.2% was observed in a temperature
range of 100°C or lower, crystallization water was contained.
[0070] From the results obtained by performing X-ray diffractometry, diffraction peak was
observed in the vicinity of each of the positions respectively corresponding to 8.5°,
15.0°, 17.4°, 21.3°, 23.2°, 26.3°, 27.7°, 28.7°, 32.8°, 34.1°, 58.6°, and 59.4° in
terms of 2θ.
[0071] From the results described above, the composition ratios, and the charge balance,
it was clarified that a crystal-structured substance expressed by Zn
4(SO
4)
0.95(CO
3)
0.05(OH)
6·3.3H
2O was contained.
[0072] Close analysis of film was performed on No. 39.
[0073] From the results obtained by performing gas chromatography mass spectrometry, it
was clarified that, since CO
2 emission was observed in a temperature range of 150°C to 500°C, C existed in the
form of carbonates.
[0074] From the results of the analysis using an X-ray photoelectron spectrometer, it was
clarified that, since a peak corresponding to Zn-LMM was observed in the vicinity
of 987 eV, Zn existed in the form of zinc hydroxide. Similarly, it was clarified that,
since a peak corresponding to S-2p was observed in the vicinity of 171 eV, S existed
in the form of sulfates.
[0075] From the results of the analysis using an X-ray-absorption fine-structure spectrometer,
it was clarified that, since peaks were observed in the vicinity of each of 2153 eV,
2158 eV, and 2170 eV, P existed in the form of pyrophosphates.
[0076] From the results of the analysis using a differential thermogravimetric analyzer,
it was clarified that, since a decrease in weight by 9.4% was observed in a temperature
range of 100°C or lower, crystallization water was contained.
[0077] From the results obtained by performing X-ray diffractometry, diffraction peak was
observed in the vicinity of each of the positions respectively corresponding to 8.8°,
15.0°, 17.9°, 21.3°, 23.2°, 27.0°, 29.2°, 32.9°, 34.7°, and 58.9° in terms of 2θ.
[0078] From the results described above, the composition ratios, and the charge balance,
it was clarified that a crystal-structured substance expressed by Zn
4(SO
4)
0.8(CO
3)
0.2(OH)
6·2.7H
2O was contained.