METHOD FOR MANUFACTURING OF HIGH STRENGTH COLD ROLLED STEEL SHEET OF EXCELLENT PHOSPHATABILITY

Abstract
A method for the manufacturing of high strength cold rolled steel sheets includes continuously annealing a cold rolled steel sheet that has a composition containing C: 0.05-0.3% mass, Si: 0.6-3.0% mass, Mn: 1.0-3.0% mass, P: 0.1% mass, S: ≦0.02% mass, Al: 0.01-1% mass, N: ≦0.01% mass, and Fe and inevitable impurities: balance, in a manner such that the cold rolled steel sheet is heated in a furnace using an oxidizing burner to a steel sheet temperature of ≧700° C., then soak-annealed in a reducing atmosphere furnace at 750-900° C., then cooled so the average cooling rate between 500° C. and 100° C. is ≧50° C./s. High-Si cold rolled steel sheets with high strength and good phosphatability while containing Si≧0.6% are obtained without controlling conditions so as to increase the dew point in the reducing atmosphere in the soaking furnace or to increase the vapor hydrogen partial pressure ratio.
Description
TECHNICAL FIELD

The present invention relates to methods for the manufacturing of automotive high strength cold rolled steel sheets that will be subjected to chemical conversion treatment such as phosphatization before use. In particular, the methods according to the invention are suitable for the manufacturing of high-Si, high strength cold rolled steel sheets that have a tensile strength of not less than 590 MPa due to the strengthening effect of Si and have excellent processability with TS×El being not less than 18000 MPa·%.


BACKGROUND ART

The weight reduction of automobiles has recently increased demands for cold rolled steel sheets having high strength and excellent processability. An automotive cold rolled steel sheet is painted before the use thereof. Prior to the painting, the steel sheet is subjected to a chemical conversion treatment called phosphatization. Phosphatability is one of the important characteristics of cold rolled steel sheets in order to ensure adhesion of a paint as well as corrosion resistance.


Regarding the production of high strength cold rolled steel sheets, PTL 1 discloses a method for producing dual phase high tensile strength cold rolled steel sheets containing Si at 0.5 to 1.5% by mass and having a tensile strength of as high as 980 MPa.


High-Si cold rolled steel sheets achieve high strength and good processability due to the strengthening effect of Si. However, silicon oxide is formed on the outermost surface during continuous annealing that is generally carried out in a N2+H2 gas atmosphere to prevent oxidation of iron (Fe). It is known that the silicon oxide layer inhibits the formation of a chemical conversion layer and the phosphatability is deteriorated.


Regarding techniques for improving the phosphatability of high-Si cold rolled steel sheets, PTL 2 discloses a method for manufacturing cold rolled steel sheets containing, in terms of % by mass, Si at not less than 0.1% and/or Mn at not less than 1.0%, which method includes forming an oxide layer on the surface of a steel sheet at a steel sheet temperature of not less than 400° C. in an iron oxidizing atmosphere, and thereafter reducing the oxide layer on the surface of the steel sheet in an iron reducing atmosphere.


CITATION LIST
Patent Literature

PTL 1: Japanese Patent No. 3478128


PTL 2: Japanese Unexamined Patent Application Publication No. 2006-45615


SUMMARY OF INVENTION
Technical Problem

According to the method disclosed in PTL 1, the steel sheet is held at a soaking temperature in a continuous annealing step in a furnace in which the atmosphere is usually a N2+H2 gas atmosphere which does not induce oxidation of iron (Fe). However, this atmosphere does not prevent silicon from being oxidized. That is, Si contained at 0.8 to 1.5% by mass forms an oxide (SiO2) on the outermost surface of the steel sheet, and the oxide remains on the final product to deteriorate the phosphatability.


According to the method of PTL 2, Fe on the surface of the steel sheet is oxidized at 400° C. or above and thereafter the steel sheet is annealed in a N2+H2 gas atmosphere which reduces the Fe oxide. That is, the layer formed on the outermost surface is not SiO2 which deteriorates the phosphatability but is a reduced Fe layer. However, when the steel sheet contains Si at 0.6% or more and the oxidation is carried out at low temperatures ranging from 400° C. to 550° C., Fe is not sufficiently oxidized due to the high effects of Si to suppress the oxidation of Fe. As a result, the formation of a reduced Fe layer on the outermost surface becomes insufficient, and the Si oxide remains on the surface of the steel sheet after the reduction to possibly deteriorate the phosphatability. Further, PTL 2 evaluates the phosphatability based only on the amount of attached phosphate. However, a study by the present inventors has revealed that not only the amount of attached phosphate but the ratio of the phosphate layer covering the steel sheet surface are influential on the adhesion of a paint and the corrosion resistance.


The present invention is aimed at solving the problems described above. It is therefore an object of the invention to provide methods for the manufacturing of high strength cold rolled steel sheets that have excellent phosphatability while containing Si at 0.6% or more.


Solution to Problem

The present invention solves the aforementioned problems by providing the following.


[1] A method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability, including continuously annealing a cold rolled steel sheet that has a composition containing:


C: 0.05 to 0.3% by mass,


Si: 0.6 to 3.0% by mass,


Mn: 1.0 to 3.0% by mass,


P: not more than 0.1% by mass,


S: not more than 0.02% by mass,


Al: 0.01 to 1% by mass,


N: not more than 0.01% by mass, and


Fe and inevitable impurities: balance,


in a manner such that the cold rolled steel sheet is heated in a furnace using an oxidizing burner to a steel sheet temperature of not less than 700° C., thereafter the steel sheet is soak-annealed in a reducing atmosphere furnace at 750 to 900° C., and the steel sheet is cooled in a manner such that the average cooling rate between 500° C. and 100° C. is not less than 50° C./s.


[2] A method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability, including continuously annealing a cold rolled steel sheet that has a composition containing:


C: 0.05 to 0.3% by mass,


Si: 0.6 to 3.0% by mass,


Mn: 1.0 to 3.0% by mass,


P: not more than 0.1% by mass,


S: not more than 0.02% by mass,


Al: 0.01 to 1% by mass,


N: not more than 0.01% by mass, and


Fe and inevitable impurities: balance,


in a manner such that the cold rolled steel sheet is heated to a steel sheet temperature of not less than 700° C. in a manner such that the steel sheet is heated in a furnace using an oxidizing burner at least when the steel sheet temperature is elevated from 600° C. to 700° C., thereafter the steel sheet is soak-annealed in a reducing atmosphere furnace at 750 to 900° C., and the steel sheet is cooled in a manner such that the average cooling rate between 500° C. and 100° C. is not less than 50° C./s.


[3] A method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability, including continuously annealing a cold rolled steel sheet that has a composition containing:


C: 0.05 to 0.3% by mass,


Si: 0.6 to 3.0% by mass,


Mn: 1.0 to 3.0% by mass,


P: not more than 0.1% by mass,


S: not more than 0.02% by mass,


Al: 0.01 to 1% by mass,


N: not more than 0.01% by mass, and


Fe and inevitable impurities: balance,


in a manner such that the cold rolled steel sheet is heated in a manner such that the steel sheet is heated in a furnace using an oxidizing burner at least from before the steel sheet temperature reaches 550° C. and further heated to a steel sheet temperature of not less than 750° C. in a furnace using a direct flame burner that is located after the oxidizing burner and has an air ratio of not more than 0.89, thereafter the steel sheet is soak-annealed in a reducing atmosphere furnace at 750 to 900° C., and the steel sheet is cooled in a manner such that the average cooling rate between 500° C. and 100° C. is not less than 50° C./s.


[4] The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to any one of [1] to [3], wherein the steel sheet further contains one or two or more of:


Ti: 0.001 to 0.1% by mass,


Nb: 0.001 to 0.1% by mass, and


V: 0.001 to 0.1% by mass.


[5] The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to any one of [1] to [4], wherein the steel sheet further contains one or two or more of:


Mo: 0.01 to 0.5% by mass, and


Cr: 0.01 to 1% by mass.


[6] The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to any one of Claims 1 to 5, wherein the steel sheet further contains:


B: 0.0001 to 0.003% by mass.


[7] The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to any one of [1] to [6], wherein the steel sheet further contains one or two or more of:


Cu: 0.01 to 0.5% by mass, and


Ni: 0.01 to 0.5% by mass.


[8] The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to any one of [1] to [7], wherein after the cooling step described in any one of [1] to [3], the steel sheet is reheated to 150 to 450° C. and soak-heat treated at the temperature for 1 to 30 minutes.


Advantageous Effects of Invention

According to the present invention, Fe on the surface of a high strength cold rolled steel sheet containing Si at 0.6% or more is oxidized and thereafter reduced to confine the Si oxide inside the steel sheet. The resultant high-Si cold rolled steel sheet achieves improved phosphatability as well as a high tensile strength of not less than 590 MPa and excellent processability with TS×El being not less than 18000 MPa·%. According to the inventive methods, it is not necessary to control the annealing atmosphere (in particular, controlling the dew point high). The inventive methods are thus advantageous in terms of operation controlling properties. Further, the inventive methods remedy the problems such as quick degradation of furnace walls or furnace rolls, and generation of scale defects or otherwise called pickups on the surface of the steel sheets.







DESCRIPTION OF EMBODIMENTS

Hereinbelow, there will be described the reason why the chemical composition of the steel sheet used in the invention is limited. The percentages [%] regarding the composition refer to % by mass unless otherwise mentioned.


Si: 0.6 to 3.0%


Silicon is an element that increases the strength without a marked decrease in processability of a steel sheet. In order to obtain a high strength cold rolled steel sheet, Si is contained at 0.6% or more. To obtain good processability, Si is preferably contained at 0.8% or more, and more preferably in excess of 1.10%. The upper limit is 3.0%, above which the steel sheet becomes very brittle.


C: 0.05 to 0.3%


In order to control the metal phase to a ferrite-martensite phase and to obtain a desired quality of the material, carbon is contained at 0.05 to 0.3%, preferably not less than 0.07%, and more preferably not less than 0.10%.


Mn: 1.0 to 3.0%


Manganese is an important element for inhibiting the formation of ferrite in a gradual cooling zone in a continuous annealing furnace. The inhibitory effect is insufficient if the manganese content is less than 1.0%. The Mn content is preferably not less than 1.5%. If the content is in excess of 3.0%, the slab cracks during a continuous casting step. The Mn content is therefore controlled to be in the range of 1.0 to 3.0%.


P: Not More than 0.1%


Phosphorus is an impurity in the steel in the present invention. Because phosphorus decreases spot weldability, it is desirable that as much as possible phosphorus be removed during steelmaking steps. If the P content is in excess of 0.1%, the spot weldability is markedly deteriorated. Thus, the P content should be not more than 0.1%.


S: Not More than 0.02%


Sulfur is an impurity in the steel in the present invention. Because sulfur decreases spot weldability, it is desirable that as much as possible sulfur be removed during steelmaking steps. If the S content is in excess of 0.02%, the spot weldability is markedly deteriorated. Thus, the S content should be not more than 0.02%. To achieve good processability, the S content is more preferably not more than 0.002%.


Al: 0.01 to 1%


Aluminum is added for the purposes of deoxidation and precipitating nitrogen as AlN. If Al is added at less than 0.01%, sufficient effects cannot be obtained in deoxidation and denitrification. Adding aluminum in an amount exceeding 1% is not economical because the effects are saturated. Thus, the Al content is controlled to be in the range of 0.01 to 1%.


N: Not More than 0.01%


Nitrogen is an impurity that is present in crude steel and decreases shaping properties of the material steel sheet. It is therefore desirable that as much as possible nitrogen be removed and the N content be reduced to the least level during steelmaking steps. However, removing nitrogen more than necessary increases refining costs. Thus, the N content is controlled to be not more than 0.01%, at which substantially no problems are caused.


Further, one or more of the following components may be added as required.


One or Two or More of Ti: 0.001 to 0.1%, Nb: 0.001 to 0.1% and V: 0.001 to 0.1%


Titanium, niobium and vanadium may be added as required because they are effective in increasing the strength by forming carbides and nitrides. When they are added, amounts of less than 0.001% do not provide sufficient effects. On the other hand, adding these elements each in excess of 0.1% results in a marked decrease in processability. Therefore, the addition amount of each of these elements is controlled to be in the range of 0.001 to 0.1%.


One or Two or More of Mo: 0.01 to 0.5% and Cr: 0.01 to 1%


Molybdenum and chromium may be added as required because they are effective in increasing the strength by inhibiting the formation of ferrite and bainite during cooling in the continuous annealing step. When they are added, amounts of less than 0.01% each do not provide sufficient effects. On the other hand, adding Mo in excess of 0.5% or Cr in excess of 1% results in a marked decrease in processability. Therefore, the addition amounts of these elements are controlled to be in the range of 0.01 to 0.5% for molybdenum and 0.01 to 1% for chromium.


B: 0.0001 to 0.003%


Boron may be added as required. When the steel sheet is used as a machinery structural member such as an automotive skeleton part, boron contributes to an increase of strength that is exhibited when the steel sheet is pressed or bake finished. The addition does not provide sufficient effects when the amount is less than 0.0001%. Adding boron in excess of 0.003% results in a marked decrease in processability. Therefore, the addition amount is controlled to be in the range of 0.0001 to 0.003%.


One or Two or More of Cu: 0.01 to 0.5% and Ni: 0.01 to 0.5%


Copper and nickel may be added as required in order to increase the strength and to inhibit corrosion during the use of the steel sheet. The addition does not provide sufficient effects when the amounts are each less than 0.01%. Adding these elements each in excess of 0.5% results in a decrease in processability as well as in yield due to the embrittlement of the steel in the manufacturing steps such as a hot rolling step. Therefore, the addition amounts are each controlled to be in the range of 0.01 to 0.5%.


The balance after the deduction of the above elements is represented by Fe and inevitable impurities.


Next, the manufacturing methods will be described.


The steel having the aforementioned composition is hot rolled, subsequently pickled and cold rolled. Thereafter, the cold rolled steel is continuously annealed on a continuous annealing line. The procedures before the continuous annealing, namely, the process for the manufacturing of the cold rolled steel sheet, is not particularly limited and a known process may be used.


In the continuous annealing line, three steps of temperature increasing, soaking and cooling are continuously carried out.


In the temperature increasing step, the steel sheet at room temperature is heated in a heating furnace using oxidizing burners to a steel sheet temperature of not less than 700° C., preferably not less than 760° C. As a result of the heating, Fe oxide is formed on the surface of the steel sheet. From the viewpoint of the formation of Fe oxide, it is preferable that the temperature be increased to as high a temperature as possible. However, excessive oxidation should be avoided because the Fe oxide falls or separates in a subsequent reducing atmosphere furnace and causes pickup defects. Accordingly, the temperature is preferably increased to not more than 800° C.


Herein, the oxidizing burner is a direct flame burner which heats a steel sheet by applying directly to the surface of the steel sheet a burner flame that is produced by burning a mixture of air and a fuel such as coke oven gas (COG) by-produced in a steelmaking plant, and in which the air ratio is increased enough to promote the oxidation of the steel sheet that is heated.


In most cases of the continuous annealing line, the heating furnace has direct flame burners. For the direct flame burners to work as oxidizing burners, the air ratio in the direct flame burners should be 0.95 or more. The air ratio is preferably 1.00 or more, and more preferably 1.10 or more. The higher the air ratio, the higher the oxidizing power. Thus, from the viewpoint of the formation of Fe oxide, it is preferable that the air ratio be as high as possible. However, excessive oxidation should be avoided because the Fe oxide falls or separates in a subsequent reducing atmosphere furnace and causes pickup defects. Accordingly, the air ratio is preferably not more than 1.3.


Examples of the fuels used in the direct flame burners include COG and liquefied natural gas (LNG).


In the case where a preheating furnace is provided before the heating furnace, the steel sheet at room temperature is heated in the preheating furnace to a steel sheet temperature of less than 600° C., and subsequently the steel sheet is heated in the heating furnace using the oxidizing burners at least from 600° C. to a steel sheet temperature of not less than 700° C. The atmosphere in the preheating furnace is not particularly limited. The preheating furnace usually utilizes residual heat of a high temperature atmosphere gas generated in the furnace. Thus, the atmosphere in the preheating furnace may be an exhaust gas from, for example, the direct flame heating zone. When the temperature of the steel sheet heated in the preheating furnace is less than 550° C., the surface of the steel sheet is not substantially oxidized and thus the atmosphere in the furnace around this temperature hardly influences the phosphatability of the product. On the other hand, Fe oxide is markedly formed on the surface of the steel sheet at a temperature of 600° C. or above. Therefore, in order to take advantage of the mechanism of improvement in phosphatability utilizing oxidation and subsequent reduction of Fe according to the finding of the present invention, it is necessary that heating be performed using the oxidizing burners at least in the range of temperatures from 600° C. to 700° C. To increase the effects by heating, the temperature is preferably raised to 760° C. or above. However, excessive oxidation should be avoided because the Fe oxide falls or separates in a subsequent reducing atmosphere furnace and causes pickup defects. Accordingly, the steel sheet is preferably heated with the oxidizing burners to a steel sheet temperature of not more than 800° C.


In order to prevent pickup defects due to the separation of Fe oxide, the heating furnace having direct flame burners is often operated in a manner such that the burners in the former stage in the heating furnace are used as oxidizing burners, and the air ratio in the latter stage in the heating furnace is controlled to be not more than 0.89 for the burners to be used as direct flame burners. Little or no oxidation takes place during heating with the burners at an air ratio of not more than 0.89. Accordingly, in the above case, heating with the oxidizing burners is initiated at least before the steel sheet temperature reaches 550° C. in order to increase the amount of Fe oxide produced in the heating furnace. That is, the steel sheet is heated in the furnace using the oxidizing burners at least after the steel sheet temperature reaches 550° C., preferably while the temperature is between 550° C. and 700° C., to form Fe oxide on the surface of the steel sheet, and thereafter the steel sheet is heated in the furnace using the direct flame burners at an air ratio of not more than 0.89 to a steel sheet temperature of not less than 750° C., and preferably not less than 760° C. Because excessive oxidation results in falling or separation of the Fe oxide in a subsequent reducing atmosphere furnace and consequent pickup defects, the steel sheet is preferably heated with the direct flame burners at an air ratio of not more than 0.89 to a steel sheet temperature of not more than 800° C.


The reducing atmosphere furnace after the heating with the oxidizing burners is a furnace equipped with a radiant tube burner. The atmosphere gas that is introduced into the furnace is preferably a mixture of H2 (1 to 10% by volume) and the balance of N2. If the volume of H2 is less than 1%, the amount of H2 is insufficient to reduce the Fe oxide on the surface of the steel sheet that is continuously passed through the furnace. With a hydrogen volume of above 10%, the reduction of Fe oxide is saturated and the excess H2 is wasted. If the dew point is above −25° C., marked oxidation with oxygen of H2O in the furnace occurs resulting in excessive internal oxidation of Si. Accordingly, the dew point is preferably not more than −25° C. Under these conditions, the atmosphere in the soaking furnace becomes reductive for Fe and the Fe oxide formed in the heating furnace is reduced. At this time, part of the oxygen atoms separated from Fe by the reduction diffuse into the steel sheet and react with Si to form the internal oxide SiO2. Because Si is oxidized inside the steel sheet and the amount of Si oxide on the outermost surface of the steel sheet on which the chemical conversion reaction takes place is reduced, the outermost surface of the steel sheet achieves good phosphatability.


The soak-annealing is performed at a steel sheet temperature in the range of 750° C. to 900° C. The soaking time is preferably 10 seconds to 10 minutes. After the soak-annealing, the steel sheet is cooled to a temperature of 100° C. or below by means of, for example, gas, mist quench (mist) or water in a manner such that the average cooling rate between 500° C. and 100° C. is not less than 50° C./s. To further improve processability (TS×El), a tempering treatment may be performed thereafter as required in which the metal sheet is soaked at 150° C. to 450° C. for 1 to 30 minutes. After the cooling or the tempering treatment, the steel sheet may be pickled with, for example, hydrochloric acid or sulfuric acid to remove oxides and other unwanted matters on the surface.


To promote the formation of phosphate crystal during the phosphatization and to achieve improved phosphatability, the surface of the steel sheet may be coated with Ni in an amount of deposited Ni of 5 mg/m2 to 100 mg/m2.


EXAMPLE 1

Steels A to N that had the chemical compositions shown in Table 1 were each hot rolled, pickled and cold rolled by ordinary methods to give steel sheets 1.5 mm in thickness. The steel sheets were each annealed by being passed through a continuous annealing line which had a heating furnace equipped with direct flame burners, a radiant tube type soaking furnace and a cooling furnace, thereby manufacturing high strength cold rolled steel sheets. Carbon gas was used as the fuel in the direct flame burners, and the air ratio was changed to various values. Table 2 describes the conditions in the heating furnace and those in the soaking furnace. After the soak-annealing, the steel sheet was cooled to not more than 100° C. by means of water, mist quench (mist) or gas at a cooling rate shown in Table 2. The holding temperature and the holding time described in Table 2 indicate that the steel sheet cooled to not more than 100° C. was reheated to the holding temperature and held for the time described in Table 2. Further, the steel sheets were pickled with the acid described in Table 2 or were directly obtained as products.


The pickling conditions were as follows.


Pickling with hydrochloric acid: acid concentration 1 to 20%, liquid temperature 30 to 90° C., pickling time 5 to 30 sec


Pickling with sulfuric acid: acid concentration 1 to 20%, liquid temperature 30 to 90° C., pickling time 5 to 30 sec


The high strength cold rolled steel sheets were evaluated with respect to phosphatability, surface appearance and mechanical properties. The methods for the evaluation of phosphatability, surface appearance and mechanical properties are described below.


(1) Phosphatability


The steel sheet was phosphated as described below using a phosphatization liquid (PALBOND (PB) L3080 (registered trademark)) manufactured by Nihon Parkerizing Co., Ltd.


The steel sheet was degreased with degreasing liquid FINE CLEANER (registered trademark) manufactured by Nihon Parkerizing Co., Ltd., and was thereafter washed with water. Subsequently, the surface of the steel sheet was conditioned for 30 seconds with surface conditioning liquid PREPAREN Z (registered trademark) manufactured by Nihon Parkerizing Co., Ltd. The steel sheet was then soaked in the phosphatization liquid (PALBOND (PB) L3080) at 43° C. for 120 seconds, washed with water and dried with hot air.


The phosphate layer was observed with a scanning electron microscope (SEM) at ×500 magnification with respect to five fields of view that were randomly selected. The none covered area ratio of the phosphate layer was measured by image processing. The following evaluation was made on the basis of the none covered area ratio. The symbols ◯ and ⊙ indicate acceptable levels. The term “none covered area” refers to the area where phosphate crystal is NOT formed. The none covered area ratio is obtained from (none covered area)/(observed area).


⊙: not more than 5%


◯: more than 5% to not more than 10%


×: more than 10% (2) Mechanical Properties


A JIS No. 5 test piece (JIS Z 2201) was sampled from the steel sheet along a direction that was perpendicular to the rolling direction. The test piece was tested in accordance with JIS Z 2241 to evaluate mechanical properties. To evaluate the strength after bake finishing, the test piece was preliminarily strained 5%, held at 170° C. for 20 minutes and stretched to determine the tensile strength (TSBH). This tensile strength was compared with the initial tensile strength (TS0), and the difference was defined as ΔTS (TSBH−TS0). The processability was evaluated based on the value obtained by tensile strength TS×elongation (El). The samples that gave a TS×El value of 18000 MPa·% or more were evaluated to be excellent in processability.


Table 2 shows the steels used in this EXAMPLE, the manufacturing conditions in the continuous annealing line and the evaluation results.









TABLE 1







unit: mass %






















Steel symbol
C
Si
Mn
P
S
Al
N
Ti
Nb
V
Cr
Mo
Cu
Ni
B

























A
0.12
1.43
1.9
0.02
0.003
0.01
0.004










B
0.08
1.62
2.5
0.01
0.002
0.03
0.003
0.03






0.0013


C
0.15
0.85
1.6
0.02
0.005
0.02
0.005

0.05

0.35


D
0.05
0.56
1.1
0.03
0.001
0.05
0.004
0.01

0.05

0.12


E
0.20
1.51
2.5
0.02
0.002
0.01
0.007
0.05


0.01
0.01


0.0033


F
0.10
1.15
2.1
0.03
0.015
0.03
0.004

0.005
0.01




0.0003


G
0.04
1.20
1.2
0.01
0.002
0.03
0.005


H
0.25
1.30
2.9
0.02
0.003
0.04
0.003


I
0.15
0.40
1.6
0.02
0.001
0.03
0.003

0.02


J
0.09
2.89
1.8
0.01
0.002
0.45
0.002





0.4
0.2


K
0.08
3.15
1.6
0.03
0.004
0.04
0.003


L
0.06
1.80
0.9
0.02
0.004
0.03
0.003







0.0005


M
0.13
2.60
3.1
0.01
0.003
0.05
0.005


N
0.12
1.30
2.0
0.01
0.002
0.03
0.004







0.0008



















TABLE 2









Heating with furnace having





direct flame burners
Conditions in reducing atmosphere annealing, cooling and reheating























Temperature
Hydrogen
Dew
Soaking
Soaking

Cooling
Holding
Holding



Steel
Air
Oxidizing
on furnace
concentration
point
temperature
time
Cooling
rate
temperature
time


No.
symbol
ratio
burners
exit side (° C.)
(% by volume)
(° C.)
(° C.)
(sec)
conditions
(° C./sec)
(° C.)
(sec)





1
A
1.00

700
6%
−28
830
30
Water
>1000




2
A
0.95

730
1%
−35
830
30
Water
>1000




3
A
1.25

800
3%
−40
830
540
Water
>1000
310
290


4
A
0.85
X
700
6%
−42
830
30
Water
>1000
350
 90


5
A
1.00

460
6%
−45
830
30
Water
>1000
220
250


6
B
1.20

800
7%
−38
820
20
Gas
100
320
650


7
B
1.00

700
7%
−38
820
20
Gas
100




8
C
1.10

760
5%
−30
800
60
Mist
500
360
670











quench


9
C
1.20

780
5%
−30
800
60
Mist
500













quench


10
D
0.96

700
3%
−25
800
120
Water
>1000
240
900


11
E
1.10

770
10% 
−45
800
100
Gas
60




12
F
1.05

760
7%
−35
850
120
Mist
500
150
460











quench


13
F
1.15

650
7%
−38
820
20
Mist
500
360
330











quench


14
G
1.00

800
6%
−42
830
20
Water
>1000
370
450


15
H
0.95

700
6%
−42
780
60
Gas
60
180
100


16
I
0.85
X
760
7%
−38
830
90
Gas
100
290
950


17
J
1.00

780
7%
−38
890
100
Water
>1000
330
570


18
K
1.20

700
5%
−30
820
140
Water
>1000
320
750


19
L
1.00

770
5%
−30
750
50
Water
>1000
260
620


20
M
1.10

760
3%
−25
800
120
Gas
100
350
140


21
N
1.20

730
10% 
−45
780
50
Water
>1000
210
140


22
D
0.87
X
800
7%
−35
750
40
Water
>1000
340
370


23
B
1.00

700
7%
−38
820
20
Gas
30















None covered












Mechanical properties
area ratio




















YS
TS

TS × EI
Δ TS
of phosphate




No.
Pickling
(MPa)
(MPa)
EI %)
(Mpa · %)
(MPa)
layer







1
Hydrochloric
810
1020
18.2
18600
20

Inventive




acid



2
Sulfuric acid
800
1010
18.9
19120
0

Inventive



3
Hydrochloric
810
1020
18.5
18820
40

Inventive




acid



4
Sulfuric acid
820
1030
18.7
19230
40
X
Comparative



5

840
1050
18.5
19470
40
X
Comparative



6

670
840
23.0
19360
10

Inventive



7
Hydrochloric
680
860
22.5
19390
20

Inventive




acid



8

830
1040
17.5
18250
40

Inventive



9
Hydrochloric
800
1000
19.6
19570
10

Inventive




acid



10
Sulfuric acid
600
750
26.5
19910
30

Inventive



11

1000
1250
15.5
19430
40

Inventive



12
Hydrochloric
790
990
19.0
18830
10

Inventive




acid



13
Sulfuric acid
820
1035
17.9
18500
0
X
Comparative



14

420
530
34.5
18260
10

Comparative



15

1200
1500
12.2
18290
30

Inventive



16
Hydrochloric
800
1000
14.3
14300
30

Comparative




acid



17
Hydrochloric
680
850
25.0
21250
0

Inventive




acid



18
Sulfuric acid
680
860
24.5
21070
10
X
Comparative



19
Sulfuric acid
430
490
39.0
19110
40

Comparative



20

1150
1350
8.4
11340
40

Comparative



21
Hydrochloric
800
1010
19.5
19740
120

Inventive




acid



22
Sulfuric acid
820
1030
18.4
18980
10
X
Comparative



23
Hydrochloric
360
550
35.0
19250
20

Comparative




acid










The steel sheets obtained in the inventive examples achieved a tensile strength (TS) of not less than 590 MPa and excellent processability with TS×El>18000, and showed good phosphatability. The steel sheets in the comparative examples were inferior in any of tensile strength, processability and phosphatability.


EXAMPLE 2

The steels A to F that had the chemical compositions shown in Table 1 were each hot rolled, pickled and cold rolled by ordinary methods to give steel sheets 1.5 mm in thickness. The steel sheets were each annealed by being passed through a continuous annealing line which had a preheating furnace, a heating furnace equipped with direct flame burners, a radiant tube type soaking furnace and a cooling furnace, thereby manufacturing high strength cold rolled steel sheets. Carbon gas was used as the fuel in the direct flame burners, and the air ratio was changed to various values. Table 3 describes the conditions in the heating furnace and those in the soaking furnace. After the soak-annealing, the steel sheet was cooled to not more than 100° C. by means of water, mist quench or gas at a cooling rate shown in Table 3. The holding temperature and the holding time described in Table 3 indicate that the steel sheet cooled to not more than 100° C. was reheated to the holding temperature and held for the time described in Table 3. Further, the steel sheets were pickled with the acid described in Table 3 or were directly obtained as products.


The pickling conditions were the same as those described in EXAMPLE 1.


The high strength cold rolled steel sheets were evaluated with respect to mechanical properties and phosphatability. The methods for the evaluation of mechanical properties and phosphatability were the same as those described in EXAMPLE 1.


Table 3 shows the steels used in this EXAMPLE, the manufacturing conditions in the continuous annealing line and the evaluation results.













TABLE 3










Heating with furnace having






direct flame burners
Conditions in reducing atmosphere annealing, cooling and reheating






















Finish


Temperature





Cooling





Steel
preheating

Oxi-
on furnace
Hydrogen
Dew
Soaking
Soaking
Cooling
rate
Holding
Holding



sym-
temperature
Air
dizing
exit side
concentration
point
temperature
time
condi-
(° C./
temperature
time


No.
bol
(° C.)
ratio
burners
(° C.)
(% by volume)
(° C.)
(° C.)
(sec)
tions
sec)
(° C.)
(° C.)





1
A
400
1.00

700
6%
−28
890
30
Water
>1000




2
A
550
0.95

730
1%
−35
860
30
Water
>1000




3
A
200
1.25

760
3%
−40
830
540
Water
>1000
320
540


4
A
620
0.95

700
6%
−42
830
30
Water
>1000
380
100


5
A
250
1.00

480
6%
−45
830
30
Water
>1000
250
590


6
A
500
0.82
X
700
10% 
−45
830
30
Water
>1000
390
440


7
B
450
1.20

780
8%
−40
820
30
Gas
100
350
430


8
C
500
1.00

700
7%
−38
820
20
Mist
500














quench


9
D
500
0.96

700
4%
−25
800
60
Water
>1000
160
150


10
E
500
1.10

800
8%
−30
750
120
Gas
60




11
F
500
1.15

760
9%
−33
850
30
Mist
500
270
270












quench


12
F
500
1.10

650
9%
−33
850
30
Mist
300
260
510












quench


13
A
500
1.00

700
5%
−25
860
160
Water
>1000




14
B
500
0.95

780
6%
−30
830
110
Water
>1000
300
740


15
C
500
1.25

700
0%
−33
860
80
Water
>1000
150
160


16
C
500
1.00

700
7%
−38
820
20
Gas
30















None covered












Mechanical properties
area ratio




















YS
TS

TS × EI
Δ TS
of phosphate




No.
Pickling
(MPa)
(MPa)
EI %)
(Mpa · %)
(MPa)
layer







1
Hydrochloric
810
1010
19.3
19520
40

Inventive




acid



2
Sulfuric acid
830
1030
19.2
19820
40

Inventive



3
Sulfuric acid
820
1020
18.0
18350
40

Inventive



4
Sulfuric acid
790
990
20.1
19920
10
X
Comparative



5
Sulfuric acid
820
1020
19.0
19350
20
X
Comparative



6
Sulfuric acid
810
1010
18.3
18470
40
X
Comparative



7

660
830
22.8
18960
10

Inventive



8
Hydrochloric
980
1230
15.5
19030
30

Inventive




acid



9
Hydrochloric
650
810
23.7
19190
40

Inventive




acid



10
Hydrochloric
1070
1340
14.9
19920
10

Inventive




acid



11

700
880
21.8
19190
0

Inventive



12
Sulfuric acid
740
920
19.6
18050
10
X
Comparative



13

800
1000
18.8
18760
30

Inventive



14
Sulfuric acid
680
850
22.2
18910
30

Inventive



15
Hydrochloric
1000
1250
15.2
19020
0
X
Comparative




acid



16
Hydrochloric
430
490
42.0
20580
30

Comparative




acid










The steel sheets obtained in the inventive examples achieved a tensile strength (TS) of not less than 590 MPa and excellent processability with TS×El>18000 MPa·%, and showed good phosphatability. The steel sheets in the comparative examples were inferior in any of tensile strength, processability and phosphatability.


EXAMPLE 3

The steels A to F, I, M and N that had the chemical compositions shown in Table 1 were each hot rolled, pickled and cold rolled by ordinary methods to give steel sheets 1.5 mm in thickness. The steel sheets were each annealed by being passed through a continuous annealing line which had a preheating furnace, a heating furnace equipped with direct flame burners, a radiant tube type soaking furnace and a cooling furnace, thereby manufacturing high strength cold rolled steel sheets. The heating furnace equipped with direct flame burners was composed of 4 zones. Carbon gas was used as the fuel in the direct flame burners, and the air ratio in the former stage (zones 1 to 3) and that in the latter stage (zone 4) in the heating furnace were changed to various values. The direct flame burners come to function as oxidizing burners at an air ratio of 0.95 or more. Table 4 describes the conditions in the heating furnace and those in the soaking furnace. After the soak-annealing, the steel sheet was cooled to not more than 100° C. by means of water, mist quench or gas at a cooling rate shown in Table 4. The holding temperature and the holding time described in Table 4 indicate that the steel sheet cooled to not more than 100° C. was reheated to the holding temperature and held for the time described in Table 4. Further, the steel sheets were pickled with the acid described in Table 4 or were directly obtained as products.


The pickling conditions were the same as those described in EXAMPLE 1.


The high strength cold rolled steel sheets were evaluated with respect to mechanical properties and phosphatability. The methods for the evaluation of mechanical properties and phosphatability were the same as those described in EXAMPLE 1.


Table 4 shows the steels used in this EXAMPLE, the manufacturing conditions in the continuous annealing line and the evaluation results.












TABLE 4









Heating with furnace having




direct flame burners
Conditions in reducing atmosphere













Finish
First stage direct
Latter stage

annealing, cooling and reheating

















preheating
flame burners
direct
Temperature
Hydrogen

Soaking
Soaking




















Steel
temperature
Air
Oxidizing
flame burners
on furnace
concentration
Dew point
temperature
time
Cooling


No.
symbol
(° C.)
ratio
burners
Air ratio
exit side (° C.)
(% by volume)
(° C.)
(° C.)
(sec)
conditions





1
A
500
1.00

0.82
750
6%
−28
890
30
Water


2
A
550
0.95

0.82
750
1%
−35
860
30
Water


3
A
500
1.25

0.82
760
3%
−40
830
540
Water


4
A
200
1.00

0.82
470
6%
−42
830
30
Water


5
A
500
0.82
X
0.82
750
6%
−45
830
30
Water


6
B
500
1.20

0.89
780
10% 
−45
830
30
Gas


7
C
500
1.00

0.75
750
7%
−38
820
20
Mist













quench


8
D
500
0.96

0.85
750
4%
−25
800
60
Water


9
E
500
1.10

0.85
800
8%
−30
750
120
Gas


10
F
500
1.10

0.85
800
8%
−30
850
30
Mist













quench


11
F
500
1.10

0.85
680
8%
−30
850
30
Mist













quench


12
I
500
0.95

0.75
750
5%
−30
860
150
Water


13
M
500
1.10

0.85
800
4%
−35
810
80
Water


14
A
500
0.96

0.75
750
0%
−30
850
130
Water


15
C
580
1.10

0.85
800
6%
−32
770
60
Water


16
D
550
0.95

0.82
750
5%
−50
830
30
Water


17
N
500
1.25

0.82
760
5%
−50
830
30
Water


18
E
500
1.10

0.82
760
5%
−40
850
60
Gas


















Conditions in reducing atmosphere








annealing, cooling and reheating












Cooling

None covered
















rate
Holding
Holding

Mechanical properties
area ratio






















(° C./
temperature
time

YS
TS

TS × EI
Δ TS
of phosphate




No.
sec)
(° C.)
(sec)
Pickling
(MPa)
(MPa)
EI %)
(Mpa · %)
(MPa)
layer







1
>1000


Hydrochloric
840
1050
19.0
19920
40

Inventive







acid



2
>1000


Sulfuric acid
820
1030
18.8
19350
40

Inventive



3
>1000
210
370
Hydrochloric
800
1000
18.5
18470
10

Inventive







acid



4
>1000
210
350
Sulfuric acid
830
1040
18.2
18960
20
X
Comparative



5
>1000
360
610
Hydrochloric
820
1020
18.7
19030
40
X
Comparative







acid



6
100



650
810
23.7
19190
10

Inventive



7
500


Hydrochloric
900
1120
17.8
19920
30

Inventive







acid



8
>1000
270
500
Hydrochloric
550
690
27.8
19190
40

Inventive







acid



9
80
310
190

980
1230
14.7
18050
10

Inventive



10
500


Hydrochloric
560
700
26.8
18760
0

Inventive







acid



11
300
200
810

640
800
23.6
18910
10
X
Comparative



12
>1000
270
200
Hydrochloric
750
940
17.4
16310
30

Comparative







acid



13
>1000


Sulfuric acid
1040
1300
8.5
11050
20

Comparative



14
>1000
270
880
Hydrochioric
800
1000
19.0
18960
40
X
Comparative







acid



15
>1000
180
510
Hydrochloric
920
1150
16.7
19190
30
X
Comparative







acid



16
>1000
380
810

600
750
26.6
19920
40

Inventive



17
>1000
190
500
Hydrochloric
750
1150
16.7
19190
110

Inventive







acid



18
40



750
950
15.6
14820
20

Comparative










The steel sheets obtained in the inventive examples achieved a tensile strength (TS) of not less than 590 MPa and excellent processability with TS×El>18000 MPa·%, and showed good phosphatability. The steel sheets in the comparative examples were inferior in any of tensile strength, processability and phosphatability.


INDUSTRIAL APPLICABILITY

The methods according to the present invention can be used for the manufacturing of high-Si, high strength cold rolled steel sheets of excellent phosphatability that have a tensile strength of not less than 590 MPa and excellent processability with TS×El being not less than 18000 MPa·%.

Claims
  • 1-8. (canceled)
  • 9. A method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability, comprising continuously annealing a cold rolled steel sheet that has a composition containing: C: 0.05 to 0.3% by mass,Si: 0.6 to 3.0% by mass,Mn: 1.0 to 3.0% by mass,P: not more than 0.1% by mass,S: not more than 0.02% by mass,Al: 0.01 to 1% by mass,N: not more than 0.01% by mass, andFe and inevitable impurities: balance,in a manner such that the cold rolled steel sheet is heated in a furnace using an oxidizing burner to a steel sheet temperature of not less than 700° C., thereafter the steel sheet is soak-annealed in a reducing atmosphere furnace at 750 to 900° C., and the steel sheet is cooled in a manner such that the average cooling rate between 500° C. and 100° C. is not less than 50° C./s.
  • 10. A method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability, comprising continuously annealing a cold rolled steel sheet that has a composition containing: C: 0.05 to 0.3% by mass,Si: 0.6 to 3.0% by mass,Mn: 1.0 to 3.0% by mass,P: not more than 0.1% by mass,S: not more than 0.02% by mass,Al: 0.01 to 1% by mass,N: not more than 0.01% by mass, andFe and inevitable impurities: balance,in a manner such that the cold rolled steel sheet is heated to a steel sheet temperature of not less than 700° C. in a manner such that the steel sheet is heated in a furnace using an oxidizing burner at least when the steel sheet temperature is elevated from 600° C. to 700° C., thereafter the steel sheet is soak-annealed in a reducing atmosphere furnace at 750 to 900° C., and the steel sheet is cooled in a manner such that the average cooling rate between 500° C. and 100° C. is not less than 50° C./s.
  • 11. A method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability, comprising continuously annealing a cold rolled steel sheet that has a composition containing: C: 0.05 to 0.3% by mass,Si: 0.6 to 3.0% by mass,Mn: 1.0 to 3.0% by mass,P: not more than 0.1% by mass,S: not more than 0.02% by mass,Al: 0.01 to 1% by mass,N: not more than 0.01% by mass, andFe and inevitable impurities: balance,in a manner such that the cold rolled steel sheet is heated in a manner such that the steel sheet is heated in a furnace using an oxidizing burner at least from before the steel sheet temperature reaches 550° C. and further heated to a steel sheet temperature of not less than 750° C. in a furnace using a direct flame burner that is located after the oxidizing burner and has an air ratio of not more than 0.89, thereafter the steel sheet is soak-annealed in a reducing atmosphere furnace at 750 to 900° C., and the steel sheet is cooled in a manner such that the average cooling rate between 500° C. and 100° C. is not less than 50° C./s.
  • 12. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 9, wherein the steel sheet further contains one or two or more of: Ti: 0.001 to 0.1% by mass,Nb: 0.001 to 0.1% by mass, andV: 0.001 to 0.1% by mass.
  • 13. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 9, wherein the steel sheet further contains one or two of: Mo: 0.01 to 0.5% by mass, andCr: 0.01 to 1% by mass.
  • 14. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 9, wherein the steel sheet further contains: B: 0.0001 to 0.003% by mass.
  • 15. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 9, wherein the steel sheet further contains one or two of: Cu: 0.01 to 0.5% by mass, andNi: 0.01 to 0.5% by mass.
  • 16. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 9, wherein after the cooling step, the steel sheet is reheated to 150 to 450° C. and soak-heat treated at the temperature for 1 to 30 minutes.
  • 17. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 10, wherein the steel sheet further contains one or two or more of: Ti: 0.001 to 0.1% by mass,Nb: 0.001 to 0.1% by mass, andV: 0.001 to 0.1% by mass.
  • 18. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 11, wherein the steel sheet further contains one or two or more of: Ti: 0.001 to 0.1% by mass,Nb: 0.001 to 0.1% by mass, andV: 0.001 to 0.1% by mass.
  • 19. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 10, wherein the steel sheet further contains one or two of: Mo: 0.01 to 0.5% by mass, andCr: 0.01 to 1% by mass.
  • 20. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 11, wherein the steel sheet further contains one or two of: Mo: 0.01 to 0.5% by mass, andCr: 0.01 to 1% by mass.
  • 21. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 12, wherein the steel sheet further contains one or two of: Mo: 0.01 to 0.5% by mass, andCr: 0.01 to 1% by mass.
  • 22. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 10, wherein the steel sheet further contains: B: 0.0001 to 0.003% by mass.
  • 23. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 11, wherein the steel sheet further contains: B: 0.0001 to 0.003% by mass.
  • 24. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 12, wherein the steel sheet further contains: B: 0.0001 to 0.003% by mass.
  • 25. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 13, wherein the steel sheet further contains: B: 0.0001 to 0.003% by mass.
  • 26. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 10, wherein the steel sheet further contains one or two of: Cu: 0.01 to 0.5% by mass, andNi: 0.01 to 0.5% by mass.
  • 27. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 11, wherein the steel sheet further contains one or two of: Cu: 0.01 to 0.5% by mass, andNi: 0.01 to 0.5% by mass.
  • 28. The method for the manufacturing of high strength cold rolled steel sheets of excellent phosphatability according to claim 12, wherein the steel sheet further contains one or two of: Cu: 0.01 to 0.5% by mass, andNi: 0.01 to 0.5% by mass.
Priority Claims (1)
Number Date Country Kind
2009-176115 Jul 2009 JP national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/JP2010/062984 7/27/2010 WO 00 4/9/2012