CN102816979A - Production method of low-carbon sulfur series free-cutting steel continuous casting billet - Google Patents

Production method of low-carbon sulfur series free-cutting steel continuous casting billet Download PDF

Info

Publication number
CN102816979A
CN102816979A CN2012103066923A CN201210306692A CN102816979A CN 102816979 A CN102816979 A CN 102816979A CN 2012103066923 A CN2012103066923 A CN 2012103066923A CN 201210306692 A CN201210306692 A CN 201210306692A CN 102816979 A CN102816979 A CN 102816979A
Authority
CN
China
Prior art keywords
steel
cutting
continuous casting
continuously cast
controlled
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN2012103066923A
Other languages
Chinese (zh)
Other versions
CN102816979B (en
Inventor
罗国华
范植金
朱玉秀
王瑞敏
徐志东
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuhan Iron and Steel Co Ltd
Original Assignee
Wuhan Iron and Steel Group Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wuhan Iron and Steel Group Corp filed Critical Wuhan Iron and Steel Group Corp
Priority to CN 201210306692 priority Critical patent/CN102816979B/en
Publication of CN102816979A publication Critical patent/CN102816979A/en
Application granted granted Critical
Publication of CN102816979B publication Critical patent/CN102816979B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treatment Of Steel In Its Molten State (AREA)

Abstract

The invention relates to a production method of a low-carbon sulfur series free-cutting steel continuous casting billet. The method comprises the steps of: first placing scrap steel into a converter, then loading liquid iron into the converter; conducting top-bottom combined blowing; carrying out tapping; performing deoxygenation and alloying; implementing argon blowing treatment; conducting soft argon blowing after alloy fine adjustment; adding carbonized rice hulls into a steel ladle when the argon blowing is over; starting continuous casting when the molten steel temperature reaches 1530-1570DEG C; and employing a continuous casting process of tundish treatment, crystallizer control, secondary cooling, straightening and cutting. The invention has the characteristics that: the smelting is free of desulfurization, LF refining treatment and other processes, no steel breakout phenomenon exists in casting, the composition control is stable, the yields of S and Mn elements are both above 90%, the cutting-tool wear can be reduced during processing so as to improve the service life, the tundish has a high utilization rate, the continuous casting billet has no subcutaneous bubble, heart crack, surface crack and other defects, and is free of composition segregation, and the inclusions in the casting billet are thick, big and in a spherical shape, thus being in favor of shape control of the rolled inclusions and improvement of the steel cutting performance.

Description

A kind of working method of low carbon-sulfur series free-cutting steel continuously cast bloom
Technical field
The present invention relates to the working method of free-cutting steel, specifically belong to the working method of low carbon-sulfur series free-cutting steel continuously cast bloom.
Background technology
In recent years, machinery manufacturing industry is towards high speed, precise treatment and automation direction development, and is in order to reduce the cut cost and to enhance productivity, improve quality product, increasing to the resulfurizing series free cutting steel with excellent in machinability ability.Sulphur is that free-cutting steel is the steel grade that kind is maximum in the current free-cutting steel, output is maximum, accounts for 70% of free-cutting steel ultimate production, resulfurizing series free cutting steel seriation, stdn that developed country produces.With the cutting ability is main sulphur and the compound free-cutting steel of sulphur, and sulphur content generally between 0.20%-0.40%, is up to 0.60%; With mechanical property is main, and cutting ability is the free-cutting steel of assisting, and sulphur content is done more important member at 0.04-0.07%, 0.08%-0.13%.MnS inclusion in the resulfurizing series free cutting steel has cut off the continuity of matrix and has made the car bits easily broken; Lubricate and reduce the wearing and tearing of cutter again simultaneously; Thereby improved the cutting ability of steel; Yet MnS along the rolling direction elongation, makes the transverse mechanical performance of sulphur free-cutting steel significantly reduce in course of hot rolling, has aggravated the steel anisotropy.In order to suppress this harmful effect, can in steel, add an amount of alloying element such as selenium, tellurium, zirconium, calcium, titanium, REE etc., form new on-deformable inclusion such as MnTe; Mn (SSe) etc., be distributed in MnS around, or form the higher inclusion of (MeMn) S hardness etc.; Restriction MnS distortion also can make through control deoxygenation conditions (oxygen amount in the steel) and form (Mn, Fe) (S in the steel; O) oxysulfide is because dissolving in of oxygen significantly reduces the deformability of MnS; The inclusion long-width ratio is little, is spherical or the spindle shape, helps improving the cutting ability of steel.
Low carbon-sulfur series free-cutting steel such as U.S.'s trade mark 1213 and 1215; Japan trade mark SUM22, SUM23 and SUM25; Steel such as Germany trade mark 11SMn30 and 11SMn37; Be mainly used in make stressed less and size and smooth finish had machining component such as production such as strict household electrical appliances, instrument, office automation, IT and lathe, this type steel grade in cutting process, have lower cutting force and cutting temperature, easy chip breaking, workpiece surface finish height and cutter life high excellence cutting ability.The composition characteristic of low carbon-sulfur series free-cutting steel is in steel, to have added S, P element; S element in the steel and Mn element interaction form manganese sulfide inclusion; Utilize the manganese sulfide inclusion thing to stress concentration in the working angles and help effect such as crack propagation, improve the cutting ability of steel; P element in the steel improves ferritic intensity, thereby the embrittlement matrix improves cutting ability.
S, O content height are similar to semikilled steel, rimming steel in the low carbon-sulfur series free-cutting steel.This type of steel grade mainly adopts the mode of production of " arc melting+die casting " at the invention initial stage, and the development along with the steel-making continuous casting technology is replaced by the mode of production of " electric arc furnace/converter melting+LF secondary refining+continuous casting process " gradually.The production difficulty of this type of steel grade is big, particularly when continuous casting is produced, following problem usually occurs: the fluctuation of (1) Mn, S elemental composition is big, and Composition Control is very unstable, and silicon, aluminium deoxidation product are many, and these brittle inclusions have reduced the cutting rolled steel performance; (2) yield of alloy is low, smelts and adopts Si-Mn, the deoxidation of Mn alloy, and the Mn yield is generally below 85%, and the S yield is not high yet, generally below 80%; (3) continuous casting process difficulty often occurs that volume slag, watering property are poor, bleed-out, connects the problems such as the stove number is few of watering, and continuous casting control is bad, and strand is easy to produce problems such as serious subsurface bubble, component segregation, heart check, surface crack.
Through preliminary search; Japanese Patent JP19940117455, JP2005363816A mention the low carbon-sulfur series free-cutting steel, and it discloses employing nitrogen pick-up mode and has produced, the deficiency of its existence: the one, increase a nitrogen content in the steel greatly; Be prone to form bubble, cause slab quality not high; The 2nd, production efficiency is low, cost is high.
Chinese patent number is the CN200510024205.4 patent documentation, and it discloses the working method of a kind of low carbon high sulfur (sulphur phosphorus) easy-to-cut structural steel continuous casting billet, i.e. the process method of " electric furnace/converter+LF processing+continuous casting ".The deficiency of its existence be the steel-making cycle long, production efficiency is low, connect and to water shortcomings such as the stove number is few.
The present invention adopts the technology pattern of " converter+Argon+continuous casting ", and optimization production technology, enhances productivity, and reduces production costs, and final production goes out fine low carbon-sulfur series free-cutting steel continuously cast bloom.
Summary of the invention
The present invention is directed to and exist operational path long at present; Continuous casting process often occurs rolling up that slag, watering property are poor, bleed-out, connect and water the more deficiency of rigid oxide content that the stove number is few, influence cutting ability, and a kind of blast-melted need through desulfurization processing, the converter of directly packing into after skimming is provided; Continuous casting process is stable; Can not produce bleed-out, improve connect and to water the stove number, the working method of the low carbon-sulfur series free-cutting steel continuously cast bloom that the good rigid oxide content of continuous casting billet quality is few.
Realize the measure of above-mentioned purpose:
A kind of working method of low carbon-sulfur series free-cutting steel continuously cast bloom, its step:
1) existing steel scrap is packed in the converter, molten iron is directly packed in the converter again, the ratio control of packing into of molten iron and steel scrap is in 10:1~3;
2) carry out top bottom blowing: before oxygen blast, carry out 2 minutes confession nitrogen earlier, oxygen blast is up to end then;
3) tapping: the control tapping temperature is at 1650~1720 ℃, and the oxygen activity in the steel is 500~900ppm;
4) deoxidation and alloying: when tap to the molten steel total amount 20~40% the time, add the Si-Al-Mn alloy according to 0.05 ~ 0.50 kilogram/ppm * oxygen activity; When tap to the molten steel total amount 41~70% the time, add ferromanganese, Iron sulfuret and ferrophosphorus successively according to the steel grades design requirements and carry out alloying; When tap to the molten steel total amount 80~95% the time, add refining slags, the CaO/SiO in the refining slag according to 4~7 kilograms of/ton steel 2Ratio is controlled to be 1.0~2.0;
5) carrying out Argon handles: liquid steel temperature carries out the alloy fine setting in the time of 1590 ~ 1610 ℃;
6) carry out the soft blow argon after the alloy fine setting finishes, the time is 4~15 minutes;
7) Argon finishes, and in ladle, adds charring rice husk according to 1.15 ~ 1.55 kilograms of/ton steel;
8) when liquid steel temperature reaches 1530~1570 ℃, the beginning continuous casting;
9) continuous casting process: tundish processing → mold → two are cold → aligning → cutting; In continuous casting process and control following parameter:
A) adopt long nozzle argon envelope and the cast of tundish blowing argon, tundish molten steel face adds the low-carbon (LC) insulating covering agent according to 0.60 ~ 0.79 kilogram of/ton steel;
B) liquid level of crystallization control device is 80~85% of a mold total height, and carries out induction stirring, and electromagnetic stirrer coil center Molten Steel Flow speed control is at 0.4 ~ 1.0 meter per second;
C) casting speed of control strand is at 0.9~1.5 meter/minute;
D) add-on of crystallizer protecting residue is controlled to be 0.3 ~ 0.5 kilogram of/ton steel;
E) crystallization control device cooling water flow is at 2000 ~ 3500 liters/minute;
F) specific water of secondary cooling zone is controlled at 0.40 ~ 0.80 liter of/kilogram steel, and continuously cast bloom is controlled at 0.2 ~ 1.0 ℃/second at the average cooling rate of secondary cooling zone;
G) straightening temperature is controlled at 900 ~ 970 ℃.
It is characterized in that: the chemical composition of Si-Al-Mn alloy and weight percent content are: Si:10 ~ 17%, Al:10 ~ 18%, Mn:67 ~ 75%.
It is characterized in that: the chemical composition of refining slag finishing slag and weight percent content are: 35 ~ 49%CaO, 20 ~ 45%SiO 2, 5 ~ 25%Al 2O 3, 8 ~ 20%MgO.
It is characterized in that: rise winch to continuous casting platform before, oxygen concn is controlled at 81 ~ 150ppm in the molten steel.
It is characterized in that: the degree of depth that submerged nozzle inserts mold is 120~180 millimeters.
It is characterized in that: the CaO/SiO of low-carbon (LC) insulating covering agent 2Ratio is controlled to be 0.8 ~ 0.95.
It is characterized in that: the viscosity of crystallizer protecting residue is 0.50 ~ 0.85 pool under 1300 ℃ of conditions, CaO/SiO 2Ratio is 0.68 ~ 0.84.
The reason of some main technologic parameters of control among the present invention:
Tapping temperature: why tapping temperature is controlled at 1650 ~ 1720 ℃, is because when tapping temperature is higher than 1720 ℃, will increase greatly to smelt to consume and make easily oxygen concn rising in the molten steel; When tapping temperature during less than 1650 ℃, again less than heat supplement, after molten steel temperature reduces gradually, influence follow-up alloying and Argon technology after the tapping, pouring practice also can't direct motion.
Tapping oxygen activity: tapping oxygen activity is controlled at below the 900ppm, is because the molten steel oxygen activity is too high, and the ladle erosion degree is strengthened, and reduces ladle work-ing life, also increases the deoxidation cost simultaneously; Tapping oxygen activity is to come better control steel inclusion because need to keep a part of oxygen in the steel more than 500ppm, avoids subsequent technique to cause in the molten steel oxygen level low excessively.
Adopt the deoxidation of SiAlMn alloy, deoxidation products floats easily, and improves greatly and the yield of stable Mn, S, P alloying element, and controls the add-on of SiAlMn alloy as requested, guarantees that molten steel has suitable oxygen concn.
Rise winch to continuous casting platform before; Oxygen concn is controlled at 81 ~ 150ppm in the molten steel, be because in the molten steel hyperoxia concentration help forming thick spherical, roll the little sulfide inclusion of after strain, thereby improve the cutting ability of steel; But too high oxygen concn causes very big difficulty can for the continuous casting operation; Occur problems such as strand subsurface bubble, heart check easily, reduce slab quality, so the molten steel oxygen concn should be controlled at 81 ~ 150ppm.
The degree of depth that submerged nozzle inserts mold is 120~180 millimeters; Be that effusive molten steel makes the molten steel ground roll greatly moving easily from mouth of a river tapping hole, influences the normal inflow of molten mold flux because the mouth of a river was inserted shallowly; Also have influence on lubricating between base shell and the mould wall, be prone to cause bleed-out, volume slag; The mouth of a river is inserted too dark, and the tapping orifice flow goes out the shortage of heat that molten steel takes the molten steel face to from the mouth of a river, makes the crystallizer protecting residue fusing bad, and the melt cinder that flows between base shell and the mould wall is less, can not evenly lubricate the base shell, influences slab quality even causes bleed-out.Therefore the degree of depth of submerged nozzle insertion mold is set at 120~180 millimeters.
The specific water of secondary cooling zone is controlled at 0.40 ~ 0.80 liter of/kilogram steel, and continuously cast bloom is controlled at 0.2 ~ 1.0 ℃/second at the average cooling rate of secondary cooling zone, is because two cold-zone cooling intensity are too small; Should cause continuously cast bloom to produce problems such as bulge and bleedout; Cooling intensity is excessive, and defectives such as seriously loosening appears in continuously cast bloom heart portion easily, shrinkage cavity, heart check cause straightening temperature to reduce simultaneously; The strand high-temp plastic reduces, and forms the aligning crackle easily.
Control electromagnetic stirrer coil center Molten Steel Flow speed control is because suitable Molten Steel Flow speed helps interrupting column crystal at 0.4 ~ 1.0 meter per second, improves the strand equiaxial crystal ratio, makes molten steel component even, avoids occurring the subsurface bubble defective; Too high velocity of flow makes liquid fluctuating excessive easily, possibly form problems such as volume slag even bleed-out, therefore, should control Molten Steel Flow speed at 0.4 ~ 1.0 meter per second.
Straightening temperature is controlled at 900 ~ 970 ℃, be because the low carbon-sulfur series free-cutting steel 800 ~ be no more than between 900 ℃ and have high-temperature brittleness, straightening temperature is low excessively, is easy to generate the aligning crackle; Straightening temperature is too high, secondary cooling zone control is required too harsh, is prone to make continuously cast bloom to form heart defect, even causes industrial accident such as bleed-out.
The present invention compared with prior art, its characteristics are: (1) smelting technology is simple, and is on-the-spot workable; (2) continuous casting does not have bleed-out, and industrial accident is few; (3) owing to, cut down the consumption of energy without operations such as desulfurization, LF refining treatment; (4) Composition Control is stable, and S, Mn element yield height all can reach more than 90%; Owing to can make Si<0.02%, Al<0.003% so make silicon, aluminium deoxidation product few, reduces tool wear raising cutter life; (5) even water the stove number and can reach more than 7 stoves, thereby improved the tundish utilization ratio, reduce refractory consumption, production efficiency is improved; (6) continuously cast bloom does not have defectives such as subsurface bubble, heart check, surface crack, and the strand composition is even simultaneously, no component segregation, and cc billet surface quality is good; (7) inclusion is thick in the strand is spherical, helps rolling back inclusion morphology control, improves the cutting rolled steel performance.
Embodiment
Describe in detail in the face of the present invention down: table 1 is the tabulation of various embodiments of the present invention Performance Detection situation;
Embodiment 1
Test conditions: adopting process: converter melting → argon station Argon → curved type continuous caster continuous casting, the production cross dimensions is 200 * 200mm 2, the step of U.S.'s trade mark 1215 low carbon-sulfur series free-cutting steel continuously cast blooms is following:
1) existing steel scrap is packed in the converter, molten iron is directly packed in the converter again, the ratio control of packing into of molten iron and steel scrap is at 10:1.5;
2) carry out top bottom blowing: before oxygen blast, carry out 2 minutes confession nitrogen earlier, oxygen blast is up to end then;
3) tapping: the control tapping temperature is at 1685 ~ 1690 ℃, and the oxygen activity in the steel is 800ppm;
4) when tap to the molten steel total amount 20% the time, add 280 kilograms of Si-Al-Mn alloys according to 0.35 kilogram/ppm * 800ppm (tapping oxygen activity), the chemical composition of Si-Al-Mn alloy and weight percent content are: Si:10%, Al:15%, Mn:75%; When tap to the molten steel total amount be 55% the time, add ferromanganese, Iron sulfuret and ferrophosphorus successively according to steel grades and carry out alloying; When tap to the molten steel total amount 82% the time, add refining slag according to 4Kg/ ton steel, the chemical composition of refining slag finishing slag and weight percent content are: 37.5%CaO, 25%SiO 2, 22.5%Al 2O 3, 15%MgO, the CaO/SiO of refining slag 2Ratio is 1.5;
5) carrying out Argon handles: liquid steel temperature carries out the alloy fine setting in the time of 1590 ~ 1595 ℃;
6) carry out the soft blow argon after the alloy fine setting finishes, the time is 4.5 minutes;
7) Argon finishes, and adds charring rice husk according to 1.2 kilograms of/ton steel; Rise winch to continuous casting platform before, oxygen concn is 98ppm in the molten steel;
8) when liquid steel temperature reaches 1537~1547 ℃, begin to carry out continuous casting; Even watering the stove number reaches 9 stoves;
9) continuous casting process: tundish processing → mold → two are cold → aligning → cutting; In continuous casting process and control following parameter:
A) adopt long nozzle argon envelope and the cast of tundish blowing argon, tundish molten steel face adds CaO/SiO according to 0.61 kilogram of/ton steel 2Ratio is 0.92 low-carbon (LC) insulating covering agent;
B) liquid level of crystallization control device is 80% of a mold total height, and carries out induction stirring, and hub of a spool Molten Steel Flow speed control is at 0.6 meter per second;
C) casting speed of control strand is at 1.2 meters/minute;
D) adopting viscosity is 0.85 pool, CaO/SiO 2Ratio is 0.8 crystallizer protecting residue, and the add-on of covering slag is a 0.4kg/ ton steel;
E) the mold cooling water flow is controlled at 3000 liters/minute; The degree of depth that submerged nozzle inserts mold is 125 millimeters;
F) specific water of secondary cooling zone is controlled at 0.40 liter/kilogram, and continuously cast bloom is controlled at 0.22 ℃/second at the average cooling rate of secondary cooling zone;
G) align, straightening temperature is 965 ℃.
Embodiment 2
Test conditions: adopting process: converter melting → argon station Argon → curved type continuous caster continuous casting, the production cross dimensions is 150 * 150mm 2, the step of Japanese trade mark SUM22 low carbon-sulfur series free-cutting steel continuously cast bloom is following:
1) existing steel scrap is packed in the converter, molten iron is directly packed in the converter again, the ratio control of packing into of molten iron and steel scrap is at 10:2;
2) carry out top bottom blowing: before oxygen blast, carry out 2 minutes confession nitrogen earlier, oxygen blast is up to end then;
3) tapping: the control tapping temperature is at 1715 ~ 1720 ℃, and the oxygen activity in the steel is 800ppm;
4) when tap to the molten steel total amount 20% the time; Add 44.88 kilograms of Si-Al-Mn alloys according to 0.051 kilogram/ppm * 800ppm (tapping oxygen activity), the chemical composition of Si-Al-Mn alloy and weight percent content are: Si: Al 14%: Mn:70% 16%; When tap to the molten steel total amount 60% the time, add ferromanganese, Iron sulfuret and ferrophosphorus successively according to steel grades and carry out alloying; When tap to the molten steel total amount 90% the time, add refining slag according to 7Kg/ ton steel, the chemical composition of refining slag finishing slag and weight percent content are: 49%CaO, 25%SiO 2, 6%Al 2O 3, 20%MgO, the CaO/SiO of refining slag 2Ratio is 1.96;
5) carrying out Argon handles: liquid steel temperature carries out the alloy fine setting in the time of 1595 ~ 1600 ℃;
6) carry out the soft blow argon after the alloy fine setting finishes, the time is 9 minutes;
7) Argon finishes, and adds charring rice husk according to 1.5 kilograms of/ton steel; Rise winch to continuous casting platform before, oxygen concn is 135ppm in the molten steel;
8) when liquid steel temperature reaches 1540~1550 ℃, begin to carry out continuous casting; Even watering the stove number reaches 8 stoves;
9) continuous casting process: tundish processing → mold → two are cold → aligning → cutting; In continuous casting process and control following parameter:
A) adopt long nozzle argon envelope and the cast of tundish blowing argon, tundish molten steel face adds CaO/SiO according to 0.73 kilogram 2Ratio is 0.90 low-carbon (LC) insulating covering agent;
B) liquid level of crystallization control device is 80% of a mold total height, and carries out induction stirring, and hub of a spool Molten Steel Flow speed control is at 1.0 meter per seconds;
C) casting speed of control strand is at 1.5 meters/minute;
D) adopting viscosity is 0.55 pool, CaO/SiO 2Ratio is 0.7 crystallizer protecting residue, and the add-on of covering slag is a 0.3kg/ ton steel;
E) the mold cooling water flow is controlled at 3000 liters/minute; The degree of depth that submerged nozzle inserts mold is 170 millimeters;
F) specific water of secondary cooling zone is controlled at 0.6 liter/kilogram, and the average cooling rate of continuously cast bloom in two cold-zones is controlled at 0.65 ℃/second;
G) align 930 ℃ of straightening temperatures.
Embodiment 3
Test conditions: adopting process: converter melting → argon station Argon → curved type continuous caster continuous casting, the production cross dimensions is 220 * 220mm 2, the step of German trade mark 11SMn37 low carbon-sulfur series free-cutting steel continuously cast bloom is following:
1) existing steel scrap is packed in the converter, molten iron is directly packed in the converter again, the ratio control of packing into of molten iron and steel scrap is at 10:3;
2) carry out top bottom blowing: before oxygen blast, carry out 2 minutes confession nitrogen earlier, oxygen blast is up to end then;
3) tapping: the control tapping temperature is at 1660 ~ 1665 ℃, and the oxygen activity in the steel is 600ppm;
4) when tap to the molten steel total amount 20% the time; Add 270 kilograms of Si-Al-Mn alloys according to 0.45 kilogram/ppm * 600ppm (tapping oxygen activity), the chemical composition of Si-Al-Mn alloy and weight percent content are: Si: Al 15%: Mn:71% 14%; When tap to the molten steel total amount be 68% the time, add ferromanganese, Iron sulfuret and ferrophosphorus successively according to steel grades and carry out alloying; When tap to the molten steel total amount 93% the time, add refining slag according to 5Kg/ ton steel, the chemical composition of refining slag finishing slag and weight percent content are: 44%CaO, 40%SiO 2, 6%Al 2O 3, 10%MgO, the CaO/SiO of refining slag 2Ratio is 1.1;
5) carrying out Argon handles: liquid steel temperature carries out the alloy fine setting in the time of 1605 ~ 1610 ℃;
6) carry out the soft blow argon after the alloy fine setting finishes, the time is 15 minutes;
7) Argon finishes, and adds charring rice husk according to 1.3 kilograms of/ton steel; Rise winch to continuous casting platform before, oxygen concn is 85ppm in the molten steel;
8) when liquid steel temperature reaches 1560~1570 ℃, begin to carry out continuous casting; Even watering the stove number reaches 10 stoves;
9) continuous casting process: tundish processing → mold → two are cold → aligning → cutting; In continuous casting process and control following parameter:
A) adopt long nozzle argon envelope and the cast of tundish blowing argon, tundish molten steel face adds CaO/SiO according to 0.79 kilogram of/ton steel 2Ratio is 0.80 low-carbon (LC) insulating covering agent;
B) liquid level of crystallization control device is 80% of a mold total height, and carries out induction stirring, and hub of a spool Molten Steel Flow speed control is at 0.4 meter per second;
C) casting speed of control strand is at 1.0 meters/minute;
D) adopting viscosity is that 0.75 pool, basicity are 0.75 crystallizer protecting residue, and the add-on of covering slag is a 0.5kg/ ton steel;
E) the mold cooling water flow is controlled at 3000 liters/minute; The degree of depth that submerged nozzle inserts mold is 140 millimeters;
F) specific water of secondary cooling zone is controlled at 0.80 liter/kilogram, and continuously cast bloom is controlled at 1 ℃/second at the average cooling rate of secondary cooling zone;
G) adopt the straightening machine continuously cast bloom to be aligned 910 ℃ of straightening temperatures.
 
9 stove steel interalloy yields and Si, Al content among table 1 embodiment 1
Connect and water the stove sequence number 1 2 3 4 5 6 7 8 9
The Mn add-on, % 0.892 0.914 0.886 0.924 0.915 0.893 0.904 0.889 0.916
The Mn quantities received, % 0.836 0.842 0.831 0.882 0.872 0.856 0.854 0.837 0.904
The Mn yield, % 94 92 94 95 95 96 94 94 99
The S add-on, % 0.281 0.272 0.285 0.266 0.257 0.273 0.264 0.282 0.274
The S quantities received, % 0.276 0.256 0.271 0.249 0.238 0.254 0.240 0.260 0.258
The S yield, % 98 94 95 94 93 93 91 92 94
The P add-on, % 0.051 0.054 0.048 0.057 0.046 0.054 0.056 0.050 0.053
The P quantities received, % 0.050 0.053 0.048 0.058 0.047 0.053 0.057 0.049 0.055
The P yield, % 98 98 100 102 102 98 102 98 104
Si content, % 0.009 0.008 0.011 0.007 0.008 0.014 0.008 0.012 0.010
Al content, % 0.001 0.002 0.001 0.002 0.001 0.002 0.002 0.001 0.002
8 stove steel interalloy yields and Si, Al content among table 2 embodiment 2
Connect and water the stove sequence number 1 2 3 4 5 6 7 8
The Mn add-on, % 0.854 0.829 0.822 0.864 0.880 0.865 0.835 0.813
The Mn quantities received, % 0.811 0.796 0.773 0.795 0.801 0.813 0.802 0.756
The Mn yield, % 95 96 94 92 91 94 96 93
The S add-on, % 0.273 0.279 0.273 0.257 0.259 0.309 0.300 0.289
The S quantities received, % 0.251 0.262 0.248 0.239 0.246 0.281 0.276 0.263
The S yield, % 92 94 91 93 95 91 92 91
The P add-on, % 0.084 0.079 0.065 0.068 0.082 0.094 0.093 0.082
The P quantities received, % 0.081 0.076 0.064 0.068 0.083 0.09 0.091 0.081
The P yield, % 97 96 98 100 101 96 98 99
Si content, % 0.009 0.012 0.013 0.016 0.010 0.011 0.008 0.009
Al content, % 0.002 0.001 0.001 0.001 0.001 0.001 0.002 0.001
10 stove steel interalloy yields and Si, Al content among table 3 embodiment 3
Connect and water the stove sequence number 1 2 3 4 5 6 7 8 9 10
The Mn add-on, % 1.339 1.420 1.443 1.379 1.541 1.264 1.350 1.376 1.396 1.459
The Mn quantities received, % 1.245 1.306 1.356 1.324 1.402 1.226 1.269 1.252 1.298 1.357
The Mn yield, % 93 92 94 96 91 97 94 91 93 93
The S add-on, % 0.366 0.360 0.392 0.371 0.372 0.383 0.391 0.376 0.374 0.371
The S quantities received, % 0.351 0.342 0.361 0.338 0.342 0.356 0.368 0.357 0.348 0.341
The S yield, % 96 95 92 91 92 93 94 95 93 92
The P add-on, % 0.066 0.057 0.066 0.066 0.078 0.072 0.059 0.067 0.061 0.072
The P quantities received, % 0.063 0.056 0.067 0.064 0.075 0.068 0.056 0.062 0.059 0.071
The P yield, % 96 98 102 97 96 94 95 93 96 98
Si content, % 0.010 0.015 0.009 0.015 0.012 0.013 0.012 0.011 0.008 0.011
Al content, % 0.001 0.001 0.001 0.001 0.002 0.001 0.001 0.002 0.002 0.001
Can find out that from table 1 ~ 3 the strand Composition Control is stable, S, Mn, P element yield are high, and make Si<0.02%, and Al<0.003 makes silicon, aluminium deoxidation product few.Continuously cast bloom does not have defectives such as subsurface bubble, heart check, surface crack, and the strand composition is even simultaneously, the segregation-free problem, and surface quality is good, even waters the stove number and reaches more than 7 stoves.Inclusion particle is thick in the continuously cast bloom is spherical, is evenly distributed, roll the back steel in manganese sulfide inclusion thing long-width ratio little, the cutting rolled steel excellent property.
The foregoing description is merely the best and gives an example, and is not to be the qualification to embodiment of the present invention.

Claims (7)

1. the working method of a low carbon-sulfur series free-cutting steel continuously cast bloom, its step:
1) earlier steel scrap is packed in the converter, molten iron is directly packed in the converter again, the ratio control of packing into of molten iron and steel scrap is in 10:1~3;
2) carry out top bottom blowing: before oxygen blast, carry out 2 minutes confession nitrogen earlier, oxygen blast is up to end then;
3) tapping: the control tapping temperature is at 1650~1720 ℃, and the oxygen activity in the steel is 500~900ppm;
4) deoxidation and alloying: when tap to the molten steel total amount 20~40% the time, add the Si-Al-Mn alloy according to 0.05 ~ 0.50 kilogram/ppm * oxygen activity; When tap to the molten steel total amount 41~70% the time, add ferromanganese, Iron sulfuret and ferrophosphorus successively according to the steel grades design requirements and carry out alloying; When tap to the molten steel total amount 80~95% the time, add refining slags, the CaO/SiO in the refining slag according to 4~7 kilograms of/ton steel 2Ratio is controlled to be 1.0~2.0;
5) carrying out Argon handles: liquid steel temperature carries out the alloy fine setting in the time of 1590 ~ 1610 ℃;
6) carry out the soft blow argon after the alloy fine setting finishes, the time is 4~15 minutes;
7) Argon finishes, and in ladle, adds charring rice husk according to 1.15 ~ 1.55 kilograms of/ton steel;
8) when liquid steel temperature reaches 1530~1570 ℃, the beginning continuous casting;
9) continuous casting process: tundish processing → mold → two are cold → aligning → cutting; In continuous casting process and control following parameter:
A) adopt long nozzle argon envelope and the cast of tundish blowing argon, tundish molten steel face adds the low-carbon (LC) insulating covering agent according to 0.60 ~ 0.79 kilogram of/ton steel;
B) liquid level of crystallization control device is 80~85% of a mold total height, and carries out induction stirring, and electromagnetic stirrer coil center Molten Steel Flow speed control is at 0.4 ~ 1.0 meter per second;
C) casting speed of control strand is at 0.9~1.5 meter/minute;
D) add-on of crystallizer protecting residue is controlled to be 0.3 ~ 0.5 kilogram of/ton steel;
E) crystallization control device cooling water flow is at 2000 ~ 3500 liters/minute;
F) specific water of secondary cooling zone is controlled at 0.40 ~ 0.80 liter of/kilogram steel, and continuously cast bloom is controlled at 0.2 ~ 1.0 ℃/second at the average cooling rate of secondary cooling zone;
G) straightening temperature is controlled at 900 ~ 970 ℃.
2. the working method of a kind of low carbon-sulfur series free-cutting steel continuously cast bloom as claimed in claim 1 is characterized in that: the chemical composition of Si-Al-Mn alloy and weight percent content are: Si:10 ~ 17%, Al:10 ~ 18%, Mn:67 ~ 75%.
3. the working method of a kind of low carbon-sulfur series free-cutting steel continuously cast bloom as claimed in claim 1 is characterized in that: the chemical composition of refining slag finishing slag and weight percent content are: 35 ~ 49%CaO, 20 ~ 45%SiO 2, 5 ~ 25%Al 2O 3, 8 ~ 20%MgO.
4. the working method of a kind of low carbon-sulfur series free-cutting steel continuously cast bloom as claimed in claim 1 is characterized in that: rise winch to continuous casting platform before, oxygen concn is controlled at 81 ~ 150ppm in the molten steel.
5. the working method of the continuously cast bloom of a kind of low carbon-sulfur series free-cutting steel as claimed in claim 1 is characterized in that: the degree of depth that submerged nozzle inserts mold is 120~180 millimeters.
6. the working method of the continuously cast bloom of a kind of low carbon-sulfur series free-cutting steel as claimed in claim 1 is characterized in that: the CaO/SiO of low-carbon (LC) insulating covering agent 2Ratio is controlled to be 0.8 ~ 0.95.
7. the working method of a kind of low carbon-sulfur series free-cutting steel continuously cast bloom as claimed in claim 1 is characterized in that: the viscosity of crystallizer protecting residue is 0.50 ~ 0.85 pascal second under 1300 ℃ of conditions, CaO/SiO 2Ratio is 0.68 ~ 0.84.
CN 201210306692 2012-08-27 2012-08-27 Production method of low-carbon sulfur series free-cutting steel continuous casting billet Expired - Fee Related CN102816979B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201210306692 CN102816979B (en) 2012-08-27 2012-08-27 Production method of low-carbon sulfur series free-cutting steel continuous casting billet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201210306692 CN102816979B (en) 2012-08-27 2012-08-27 Production method of low-carbon sulfur series free-cutting steel continuous casting billet

Publications (2)

Publication Number Publication Date
CN102816979A true CN102816979A (en) 2012-12-12
CN102816979B CN102816979B (en) 2013-12-25

Family

ID=47301418

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201210306692 Expired - Fee Related CN102816979B (en) 2012-08-27 2012-08-27 Production method of low-carbon sulfur series free-cutting steel continuous casting billet

Country Status (1)

Country Link
CN (1) CN102816979B (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104959556A (en) * 2015-06-17 2015-10-07 柳州金特新型耐磨材料股份有限公司 Continuous steel casting production method
CN105682828A (en) * 2013-09-27 2016-06-15 日新制钢株式会社 Continuous casting method
CN105682825A (en) * 2013-08-26 2016-06-15 日新制钢株式会社 Continuous casting method
CN108265228A (en) * 2018-02-01 2018-07-10 湖南华菱湘潭钢铁有限公司 A kind of production method of high cutting ability steel
CN109252086A (en) * 2017-07-13 2019-01-22 鞍钢股份有限公司 Production method of high-sulfur steel
CN110904395A (en) * 2019-12-17 2020-03-24 芜湖新兴铸管有限责任公司 Sulfur-containing free-cutting steel and smelting method thereof
CN111435121A (en) * 2018-12-26 2020-07-21 山西建龙实业有限公司 Method for detecting and analyzing edge crack defect of hot-rolled steel strip
CN111763873A (en) * 2020-08-12 2020-10-13 宝武集团鄂城钢铁有限公司 Production method of low-carbon high-sulfur free-cutting steel
CN112981249A (en) * 2021-02-07 2021-06-18 成都先进金属材料产业技术研究院股份有限公司 Smelting method of electrode bar base material for protective atmosphere electroslag remelting H13 steel
CN113430449A (en) * 2021-06-24 2021-09-24 河南中原特钢装备制造有限公司 Smelting and continuous casting production process of sulfur-containing free-cutting steel ASTM1141
CN114082910A (en) * 2021-11-25 2022-02-25 山东钢铁股份有限公司 Method for inhibiting water gap from being blocked
CN114309507A (en) * 2021-12-24 2022-04-12 湖南华菱涟源钢铁有限公司 Crystallizer casting powder and application thereof
CN114433807A (en) * 2022-01-26 2022-05-06 南京钢铁股份有限公司 Continuous casting process for producing free-cutting steel by converter
CN115341131A (en) * 2022-09-13 2022-11-15 新余钢铁股份有限公司 Continuous casting method for improving yield of low-carbon steel plate continuous casting head blank
CN115852234A (en) * 2022-12-07 2023-03-28 日照钢铁控股集团有限公司 Low-cost control method for conventional plate blank weathering steel
CN115852232A (en) * 2022-11-28 2023-03-28 阳春新钢铁有限责任公司 Method for producing chalcogenide free-cutting steel by continuous casting and full water cooling
CN115885055A (en) * 2020-06-02 2023-03-31 日铁不锈钢株式会社 Ferritic stainless steel

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11310848A (en) * 1998-04-27 1999-11-09 Sumitomo Metal Ind Ltd Manufacture of continuously cast slab for high strength free cutting non-heat-treated steel product and steel product
CN101338398A (en) * 2008-08-14 2009-01-07 武汉钢铁(集团)公司 High strength non-quenched and tempered free machining steel for automobile connecting bar and technological process thereof
CN101899555A (en) * 2010-08-04 2010-12-01 武汉钢铁(集团)公司 Production method of graphitized free-machining steel

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11310848A (en) * 1998-04-27 1999-11-09 Sumitomo Metal Ind Ltd Manufacture of continuously cast slab for high strength free cutting non-heat-treated steel product and steel product
CN101338398A (en) * 2008-08-14 2009-01-07 武汉钢铁(集团)公司 High strength non-quenched and tempered free machining steel for automobile connecting bar and technological process thereof
CN101899555A (en) * 2010-08-04 2010-12-01 武汉钢铁(集团)公司 Production method of graphitized free-machining steel

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105682825A (en) * 2013-08-26 2016-06-15 日新制钢株式会社 Continuous casting method
CN105682828A (en) * 2013-09-27 2016-06-15 日新制钢株式会社 Continuous casting method
EP3050644A4 (en) * 2013-09-27 2017-04-26 Nisshin Steel Co., Ltd. Continuous casting method
US9713839B2 (en) 2013-09-27 2017-07-25 Nisshin Steel Co., Ltd. Continuous casting method
CN104959556A (en) * 2015-06-17 2015-10-07 柳州金特新型耐磨材料股份有限公司 Continuous steel casting production method
CN109252086A (en) * 2017-07-13 2019-01-22 鞍钢股份有限公司 Production method of high-sulfur steel
CN108265228A (en) * 2018-02-01 2018-07-10 湖南华菱湘潭钢铁有限公司 A kind of production method of high cutting ability steel
CN111435121A (en) * 2018-12-26 2020-07-21 山西建龙实业有限公司 Method for detecting and analyzing edge crack defect of hot-rolled steel strip
CN110904395A (en) * 2019-12-17 2020-03-24 芜湖新兴铸管有限责任公司 Sulfur-containing free-cutting steel and smelting method thereof
CN115885055A (en) * 2020-06-02 2023-03-31 日铁不锈钢株式会社 Ferritic stainless steel
CN111763873A (en) * 2020-08-12 2020-10-13 宝武集团鄂城钢铁有限公司 Production method of low-carbon high-sulfur free-cutting steel
CN112981249A (en) * 2021-02-07 2021-06-18 成都先进金属材料产业技术研究院股份有限公司 Smelting method of electrode bar base material for protective atmosphere electroslag remelting H13 steel
CN113430449B (en) * 2021-06-24 2022-10-25 河南中原特钢装备制造有限公司 Smelting and continuous casting production process of sulfur-containing free-cutting steel ASTM1141
CN113430449A (en) * 2021-06-24 2021-09-24 河南中原特钢装备制造有限公司 Smelting and continuous casting production process of sulfur-containing free-cutting steel ASTM1141
CN114082910A (en) * 2021-11-25 2022-02-25 山东钢铁股份有限公司 Method for inhibiting water gap from being blocked
CN114309507A (en) * 2021-12-24 2022-04-12 湖南华菱涟源钢铁有限公司 Crystallizer casting powder and application thereof
CN114433807A (en) * 2022-01-26 2022-05-06 南京钢铁股份有限公司 Continuous casting process for producing free-cutting steel by converter
CN115341131A (en) * 2022-09-13 2022-11-15 新余钢铁股份有限公司 Continuous casting method for improving yield of low-carbon steel plate continuous casting head blank
CN115852232A (en) * 2022-11-28 2023-03-28 阳春新钢铁有限责任公司 Method for producing chalcogenide free-cutting steel by continuous casting and full water cooling
CN115852232B (en) * 2022-11-28 2024-04-30 阳春新钢铁有限责任公司 Method for producing chalcogenide free-cutting steel by continuous casting full water cooling
CN115852234A (en) * 2022-12-07 2023-03-28 日照钢铁控股集团有限公司 Low-cost control method for conventional plate blank weathering steel
CN115852234B (en) * 2022-12-07 2024-06-25 日照钢铁控股集团有限公司 Low-cost control method for conventional slab weathering steel

Also Published As

Publication number Publication date
CN102816979B (en) 2013-12-25

Similar Documents

Publication Publication Date Title
CN102816979B (en) Production method of low-carbon sulfur series free-cutting steel continuous casting billet
CN102409236B (en) Method for producing super-thick steel plate
CN102433504B (en) Steel for medium/heavy duty vehicle gear shaft blank in cross wedge rolling process and preparation method thereof
CN103160729B (en) Medium-carbon microalloyed steel for engineering machinery caterpillar chain piece and production process thereof
CN102618782B (en) Large-specification Z-direction H-steel and preparation method thereof
CN104278197B (en) Smelting method of steel for low-silicon high-titanium welding wire
CN102021488B (en) Steel for nuclear-island seamless steel tube and production method thereof
CN103334050B (en) Process utilizing sheet billet continuous casting to manufacture low aluminum silicon calm carbon structural steel
CN101921953A (en) Production method of anti-corrosion and high strength ultra-thick steel plates
CN112080700B (en) High-sulfur low-aluminum free-cutting steel continuous casting slab and production method thereof
CN111455125B (en) Production method for increasing continuous casting heat of high-aluminum steel
CN111041352B (en) External refining production method of wire rod for cutting diamond wire
CN109988972A (en) A kind of low-carbon sulfur-bearing air conditioner tube round steel and its production technology
CN109402327B (en) External refining production method of ultrapure high-carbon chromium bearing steel
CN105908080A (en) Preparation method for high-manganese steel for ocean platform and continuous casting slab of high-manganese steel
CN102851447B (en) Outside-furnace refining production method of steel used in carbon steel welding wire
CN103834848A (en) Steel for boron-containing prestressed steel wires and steel strands and smelting process thereof
CN108893682B (en) Die steel billet and preparation method thereof
CN104928582A (en) 41Cr4 gear steel and production method thereof
CN114932338A (en) Wire rod for high-titanium gas shielded welding wire and production process thereof
CN115354213A (en) Low-carbon and low-silicon gas shielded welding wire and hot-rolled wire rod smelting method for welding rod
CN113564447B (en) Vanadium-controlled Cr13 type hydroelectric stainless steel smelting method
CN110541115A (en) Method for manufacturing austenitic stainless steel 150 short-specification continuous casting round pipe blank
CN110714161B (en) High-sulfur free-cutting steel for automobile and production process thereof
CN115821150B (en) Control method for avoiding bubble defect of welding rod steel H08A

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20170711

Address after: 430083 Qingshan District, Hubei, Wuhan factory before the door No. 2

Patentee after: Wuhan iron and Steel Company Limited

Address before: 430080 Wuhan, Hubei Friendship Road, No. 999, Wuchang

Patentee before: Wuhan Iron & Steel (Group) Corp.

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131225

Termination date: 20180827