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(11) | EP 3 159 424 A1 |
| (12) | EUROPEAN PATENT APPLICATION |
| published in accordance with Art. 153(4) EPC |
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| (54) | REBAR AND PREPARATION METHOD THEREOF |
| (57) The present invention relates to a steel rebar comprising the following ingredients:
0.005%-0.030% of C, 0.3%-0.6% of Si, 1.2%-2.5% of Mn, 0.01 % or less of P, 0.01 %
or less of S, 8.0%-10.0% of Cr, 1.0%-3.0% of Mo, 0.2%-0.4% of Sn, 0.01 %-0.05% of
Rare Earth element, and the remainder being Fe and unavoidable impurities. The present
invention also provides a production method of steel rebar. The steel rebar of the
present invention has excellent comprehensive mechanical properties and corrosion
resistance performance, while meeting the requirements of anti-knock, the service
life in sea water of the steel rebar is increased, thus it can be widely used in reinforced
concrete structures in ocean environment. |
Technical Field
Background of the Invention
Summary of the Invention
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.2%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.0%-3.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element, and
the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.2%-1.8% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.0%-1.6% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element, and
the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.2%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.0%-3.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element,
0.04%-0.18% of V and/or 0.010%-0.030% of Ti,
and the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.7%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.5%-2.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element,
0.04%-0.08% of V, and
the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.7%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.8%-3.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element,
0.10%-0.18% of V,
0.010%-0.030% of Ti, and
the remainder being Fe and unavoidable impurities.
S1: performing preliminary desulfurization of molten iron to control the sulfur content at no more than 0.01%;
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping;
S3: performing steel tapping, during the process of which, alloying elements of Si and Mn are added for deoxygenation and carbon powder and slag former are also added;
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen in an RH vacuum refining furnace so as to control the Cr and C contents within the required range; performing deoxygenation with an LF furnace, adding the required alloying elements of Mn, Mo, Sn, Rare Earth, as well as V and/or Ti, into the steel after deoxygenation, and then adding calcium-ferrum alloy under soft stirring by blowing inert gas, so as to control contents of these elements within the required range; raising the temperature of the molten steel and adding a cover agent;
S5: performing continuous casting, by casting the molten steel under protective casting with a continuous casting machine to form a continuous casting slab;
S6: performing rolling, by heating the continuous casting slab to a temperature higher than its austenitization temperature in a heating furnace, rough rolling, moderate rolling, precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling, so as to produce a finished product of steel rebar with the required ingredients.
Brief Description of the Drawings
FIG. 1 is a microstructure view of a steel rebar of the present invention.
Detailed Description of Embodiments
| C | Si | Mn | Cr | Mo | RE | Sn | V | Ti | P | S | |
| Embodiment 1 | 0.005 | 0.60 | 2.5 | 9.0 | 1.0 | 0.05 | 0.20 | - | - | <0.01 | <0.01 |
| Embodiment 2 | 0.030 | 0.45 | 1.2 | 10.0 | 3.0 | 0.01 | 0.40 | - | - | <0.01 | <0.01 |
| Embodiment 3 | 0.015 | 0.30 | 1.8 | 8.0 | 1.6 | 0.03 | 0.30 | - | - | <0.01 | <0.01 |
| Embodiment 4 | 0.020 | 0.5 | 2.3 | 8.5 | 2.2 | 0.02 | 0.25 | 0.04 | - | <0.01 | <0.01 |
| Embodiment 5 | 0.025 | 0.55 | 1.7 | 8.2 | 2.3 | 0.02 | 0.35 | 0.18 | 0.01 | <0.01 | <0.01 |
| Embodiment 6 | 0.009 | 0.35 | 1.8 | 8.5 | 2.5 | 0.04 | 0.36 | 0.1 | 0.03 | <0.01 | <0.01 |
| Embodiment 7 | 0.012 | 0.40 | 2.2 | 9.5 | 1.5 | 0.03 | 0.28 | - | 0.02 | <0.01 | <0.01 |
| Embodiment 8 | 0.012 | 0.57 | 1.8 | 9.7 | 2.0 | 0.03 | 0.21 | 0.08 | - | <0.01 | <0.01 |
| Embodiment 9 | 0.018 | 0.50 | 1.9 | 9.0 | 1.7 | 0.02 | 0.30 | 0.06 | - | <0.01 | <0.01 |
| Embodiment 10 | 0.026 | 0.50 | 2.3 | 8.1 | 1.8 | 0.05 | 0.40 | 0.15 | 0.02 | <0.01 | <0.01 |
| Comparison Example 1 | 0.23 | 0.54 | 1.5 | - | - | - | - | - | - | <0.01 | <0.01 |
| Comparison Example 2 | 0.015 | 0.48 | 1.9 | 9.1 | 1.8 | 0.02 | 0.60 | - | - | <0.01 | <0.01 |
| Comparison Example 3 | 0.024 | 0.52 | 2.0 | 9.8 | 2.0 | 0.02 | - | - | - | <0.01 | <0.01 |
Embodiment 1
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping step with a steel tapping temperature of 1680°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1605°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1575°C until the oxygen content in the molten steel reaches 40ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 5min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 1 in Table 1; raising the temperature of the molten steel to 1580°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1100°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1030°C and the precision rolling temperature at 950°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 900°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 2
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1690°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1625°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1600°C until the oxygen content in the molten steel reaches 20ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 6min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 2 in Table 1; raising the temperature of the molten steel to 1600°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1200°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1100°C and the precision rolling temperature at 1050°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 960°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 3
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1685°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1610°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1585°C until the oxygen content in the molten steel reaches 30ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 6min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 3 in Table 1; raising the temperature of the molten steel to 1570°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1120°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1050°C and the precision rolling temperature at 960°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 910°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 4
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1690°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, performed by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1620°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1590°C until the oxygen content in the molten steel reaches 20ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth, V into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 6min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 4 in Table 1; raising the temperature of the molten steel to 1585°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1180°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1040°C and the precision rolling temperature at 990°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 950°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 5
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1675°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1615°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1580°C until the oxygen content in the molten steel reaches 25ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth, V, Ti into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 7min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 5 in Table 1; raising the temperature of the molten steel to 1580°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1190°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1095°C and the precision rolling temperature at 1030°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 950°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 6
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1670°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1610°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1580°C until the oxygen content in the molten steel reaches 20ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth, V, Ti into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 7min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 6 in Table 1; raising the temperature of the molten steel to 1590°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1185°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1085°C and the precision rolling temperature at 1035°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 955°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 7
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1685°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1615°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1580°C until the oxygen content in the molten steel reaches 20ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth, Ti into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 7min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 7 in Table 1; raising the temperature of the molten steel to 1585°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1180°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1080°C and the precision rolling temperature at 1020°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 940°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 8
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1680°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1610°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1585°C until the oxygen content in the molten steel reaches 20ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth, V into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 7min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 8 in Table 1; raising the temperature of the molten steel to 1590°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1150°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1065°C and the precision rolling temperature at 1025°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 965°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 9
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1675°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1605°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1575°C until the oxygen content in the molten steel reaches 20ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth, V into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 7min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 9 in Table 1; raising the temperature of the molten steel to 1580°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1105°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1045°C and the precision rolling temperature at 1005°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 945°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Embodiment 10
S1: performing preliminary desulfurization of molten iron by using a KR method to control the sulfur content at no more than 0.01%. Because sulfur element as an impurity element would reduce mechanical properties and corrosion resistance performance of steel and normally cannot be removed in a convertor, therefore, in order to reduce the sulfur content in steel, preliminary desulfurization treatment needs to be performed in molten iron. Before performing desulfurization, the blast furnace slag needs to be removed in order to increase the desulfurization efficiency. A mixture of lime powder and fluorite mixed at a mass ratio of 9:1 is adopted as the desulfurization agent. After still standing of the desulfurated molten iron, the desulfurization residue is removed to prevent it from entering the convertor and causing convertor resulfurization. Thereby, the sulfur content in the steel is ensured to be controlled at less than 0.01%.
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping. The convertor is a top and bottom combined blown converter.
S3: performing steel tapping with a steel tapping temperature of 1685°C. During the steel tapping process, alloying elements of Si and Mn are added for deoxygenation, and carbon powder and slag former are also added. During the operation process of steel tapping, a protective gas is blown into the molten steel for stirring the molten steel at a pressure of 0.5MPa. The fluidity of the molten steel is utilized to make the deoxygenation of the added Si and Mn elements more thoroughly and to facilitate the removal of inclusions by floating. The carbon powder and slag former are added to increase the carbon content of steel and to produce reduced slag, so as to prepare for the subsequent refining procedure outside the convertor.
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen at 1620°C in an RH vacuum refining furnace, so that C element is partially removed by the decarburization process, thereby controlling the contents of Cr and C elements within the required range; performing deoxygenation with an LF furnace at 1585°C until the oxygen content in the molten steel reaches 20ppm, and adding the required alloying elements of Mn, Mo, Sn, Rare Earth, V, Ti into the steel after deoxygenation, wherein, while the added alloying elements may be a pure metallic element, normally they are added in the form of iron alloy; and then adding calcium-ferrum alloy to perform denaturation treatment on the inclusions, performing soft stirring by blowing inert gas for 7min to make the ingredients and temperature of the steel uniformly distributed and to facilitate the removal of inclusions by floating, so that the contents of the ingredients are controlled within the ranges as shown in data of Embodiment 10 in Table 1; raising the temperature of the molten steel to 1595°C during a later period of processing with the LF furnace, in order to ensure smooth operation of continuous casting, and then adding a cover agent which usually is carbonized rice husk.
S5: continuous casting, by casting the molten steel under protective casting with a continuous casting machine to produce small square billets of 150mm×150mm.
S6: performing rolling, by heating the continuous casting slab to 1195°C in a heating furnace, performing rough rolling, moderate rolling and precision rolling by using a continuous rod and wire rolling machine with the start rolling temperature at 1095°C and the precision rolling temperature at 1045°C, without passing water cooling after precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling until room temperature, thereby producing a finished product of steel rebar as shown in Table 1, wherein, the temperature when the rolled steel is initially placed onto the cooling bed is 955°C. By means of the technique of controlled rolling and controlled cooling, the microstructure of bainite plus ferrite is finally obtained.
Experimental Example
1. Experimental methods
1.1 mechanical property tests: performed according to "GB1499.2-2007, steel used in reinforced concrete, Part II: hot-rolled ribbed rebar". The yield strength (R0.2), tensile strength (Rm), and after-fracture elongation percentage (A) are tested.
1.2 corrosion resistance performance tests:
1.2.1 cyclic immersion corrosion test: performed according to "corrosion test methods
of steel rebar in a chloride ion environment, a draft for consultation" proposed by
Steel Industry Association of China and drafted by institutes of Iron and Steel Research
Institute and Metallurgical Industry Information Standardization Research Institute.
The test sample is a cylinder of ∮13mm×50mm;
The test solution is a solution of sodium chloride with an initial concentration of
(0.34±0.009)mol•L-1 (an initial mass percentage of 2.0%±0.05%). And the specific test conditions are
as follows:
Temperature: 45°C±2°C
Humidity: 70%±10% RH
PH value of solution: 6.5-7.2
Test time: 360h
Each cyclic period: 60 min±5min, with an immersion time of 12 min±2min Highest temperature of test sample surface after baking: 70°C±10°C
1.2.2 salt spray corrosion test: performed according to "GBT10125-1997, corrosion
tests in an artificial atmosphere, salt spray test".
The test sample is a test plate of 3mm×15mm×40mm;
The test solution is a solution of sodium chloride with a concentration of (50±5)g•L-1 (a mass percentage of 5.0%±0.5%). And the specific test conditions are as follows:
Temperature: 35°C±2°C
PH value of solution: 6.5-7.2
Test time: 360h
2. Experimental results
| R0.2/MPa | Rm/MPa | A/% | Rm/ R0.2 | Agt/% | |
| Embodiment 1 | 432 | 627 | 24.5 | 1.45 | 11.8 |
| Embodiment 2 | 408 | 613 | 25.3 | 1.50 | 12.6 |
| Embodiment 3 | 482 | 696 | 24.5 | 1.44 | 11.1 |
| Embodiment 4 | 561 | 728 | 18.9 | 1.30 | 10.8 |
| Embodiment 5 | 611 | 793 | 19.6 | 1.29 | 10.5 |
| Embodiment 6 | 554 | 755 | 20.8 | 1.36 | 10.3 |
| Embodiment 7 | 524 | 716 | 21.2 | 1.37 | 10.7 |
| Embodiment 8 | 523 | 743 | 25.0 | 1.42 | 11.3 |
| Embodiment 9 | 536 | 729 | 21.0 | 1.36 | 10.7 |
| Embodiment 10 | 621 | 795 | 18.0 | 1.28 | 9.5 |
| Comparison Example 1 | 435 | 632 | 22.0 | 1.45 | 12.0 |
| Comparison Example 2 | 486 | 586 | 13.4 | 1.21 | 6.2 |
| Comparison Example 3 | 477 | 687 | 24.8 | 1.44 | 11.0 |
| cyclic immersion test | salt spray test | |||||
| Corrosion rate (g/m2·h) | Relative corrosion rate | Increase of corrosion resistance performance (%) | Corrosion rate (g/m2·h) | Relative corrosion rate | Increase of corrosion resistance performance (%) | |
| Embodiment 1 | 0.415 | 0.127 | 690 | 0.411 | 0.130 | 666 |
| Embodiment 2 | 0.191 | 0.058 | 1616 | 0.205 | 0.065 | 1437 |
| Embodiment 3 | 0.419 | 0.128 | 682 | 0.432 | 0.137 | 629 |
| Embodiment 4 | 0.356 | 0.109 | 821 | 0.367 | 0.117 | 758 |
| Embodiment 5 | 0.441 | 0.135 | 643 | 0.445 | 0.141 | 608 |
| Embodiment 6 | 0.349 | 0.106 | 839 | 0.360 | 0.114 | 775 |
| Embodiment 7 | 0.386 | 0.118 | 749 | 0.395 | 0.125 | 697 |
| Embodiment 8 | 0.272 | 0.083 | 1105 | 0.288 | 0.091 | 994 |
| Embodiment 9 | 0.370 | 0.113 | 786 | 0.381 | 0.121 | 727 |
| Embodiment 10 | 0.433 | 0.132 | 657 | 0.435 | 0.138 | 624 |
| Comparison Example 1 | 3.278 | 1 | - | 3.150 | 1 | - |
| Comparison Example 2 | 0.365 | 0.111 | 798 | 0.377 | 0.120 | 736 |
| Comparison Example 3 | 0.456 | 0.151 | 561 | 0.463 | 0.160 | 526 |
| (The relative corrosion rates in Table 3 are all compared with Comparison Example 1, by setting the relative corrosion rate of Comparison Example 1 to be 1.000) |
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.2%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.0%-3.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element, and
the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.2%-1.8% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.0%-1.6% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element, and
the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.2%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.0%-3.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element, 0.04%-0.18% of V and/or 0.010%-0.030% of Ti, and the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.7%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.5%-2.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element,
0.04%-0.08% of V, and
the remainder being Fe and unavoidable impurities.
0.005%-0.030% of C,
0.3%-0.6% of Si,
1.7%-2.5% of Mn,
0.01% or less of P,
0.01% or less of S,
8.0%-10.0% of Cr,
1.8%-3.0% of Mo,
0.2%-0.4% of Sn,
0.01%-0.05% of Rare Earth element,
0.10%-0.18% of V,
0.010%-0.030% of Ti, and
the remainder being Fe and unavoidable impurities.
S1: performing preliminary desulfurization of molten iron to control the sulfur content at no more than 0.01%;
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping;
S3: performing steel tapping, during the process of which, alloying elements of Si and Mn are added for deoxygenation and carbon powder and slag former are also added;
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen in an RH vacuum refining furnace so as to control the Cr and C contents within the range in accordance with Claim 1 or 2; carrying out deoxygenation with an LF furnace, adding the required alloying elements of Mn, Mo, Sn and Rare Earth into the steel after deoxygenation, and then adding calcium-ferrum alloy under soft stirring by blowing inert gas, so as to control contents of these elements within the range in accordance with Claim 1 or 2; raising the temperature of the molten steel and adding a cover agent;
S5: performing continuous casting, by casting the molten steel under protective casting with a continuous casting machine to form a continuous casting slab;
S6: performing rolling, by heating the continuous casting slab to a temperature higher than its austenitization temperature in a heating furnace, rough rolling, moderate rolling, precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling, so as to produce a finished product of steel rebar with ingredients in accordance with Claim 1 or 2.
S1: performing preliminary desulfurization of molten iron to control the sulfur content at no more than 0.01%;
S2: performing smelting in a convertor, by feeding the molten iron processed by Step S1 together with steel scrap and/or pig iron into a convertor to be smelted, thus obtaining steel with a carbon content less than 0.05% and a phosphorus content less than 0.01% for steel tapping;
S3: performing steel tapping, during the process of which, alloying elements of Si and Mn are added for deoxygenation and carbon powder and slag former are also added;
S4: performing refining outside the convertor, by adding Cr element and meanwhile performing decarburization by blowing oxygen in an RH vacuum refining furnace so as to control the Cr and C contents within the range in accordance with Claim 3 or 4 or 5 or 6; carrying out deoxygenation with an LF furnace, adding the required alloying elements of Mn, Mo, Sn, Rare Earth, as well as V and/or Ti, into the steel after deoxygenation, and then adding calcium-ferrum alloy under soft stirring by blowing inert gas, so as to control contents of these elements within the range in accordance with Claim 3 or 4 or 5 or 6; raising the temperature of the molten steel and adding a cover agent;
S5: performing continuous casting, by casting the molten steel under protective casting with a continuous casting machine to form a continuous casting slab;
S6: performing rolling, by heating the continuous casting slab to a temperature higher than its austenitization temperature in a heating furnace, rough rolling, moderate rolling, precision rolling, and placing the rolled steel after precision rolling onto a cooling bed for air cooling, so as to produce a finished product of steel rebar with ingredients in accordance with Claim 3 or 4 or 5 or 6.
REFERENCES CITED IN THE DESCRIPTION
Patent documents cited in the description