CN116334341A - Method for producing high-chromium corrosion-resistant sucker rod steel by converter - Google Patents
Method for producing high-chromium corrosion-resistant sucker rod steel by converter Download PDFInfo
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- CN116334341A CN116334341A CN202310264319.4A CN202310264319A CN116334341A CN 116334341 A CN116334341 A CN 116334341A CN 202310264319 A CN202310264319 A CN 202310264319A CN 116334341 A CN116334341 A CN 116334341A
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- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 43
- 239000010959 steel Substances 0.000 title claims abstract description 43
- 239000011651 chromium Substances 0.000 title claims abstract description 35
- 229910052804 chromium Inorganic materials 0.000 title claims abstract description 32
- 238000005260 corrosion Methods 0.000 title claims abstract description 26
- 230000007797 corrosion Effects 0.000 title claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 27
- 238000010079 rubber tapping Methods 0.000 claims abstract description 26
- 229910000604 Ferrochrome Inorganic materials 0.000 claims abstract description 22
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 14
- 239000000956 alloy Substances 0.000 claims abstract description 14
- 238000009749 continuous casting Methods 0.000 claims abstract description 9
- 238000007670 refining Methods 0.000 claims abstract description 9
- 238000005275 alloying Methods 0.000 claims abstract description 8
- 238000005266 casting Methods 0.000 claims abstract description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 30
- 229910052799 carbon Inorganic materials 0.000 claims description 18
- 229910052786 argon Inorganic materials 0.000 claims description 15
- 238000007664 blowing Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000003795 chemical substances by application Substances 0.000 claims description 9
- 239000002893 slag Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 6
- 239000000498 cooling water Substances 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- 238000004886 process control Methods 0.000 claims description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 3
- 239000005997 Calcium carbide Substances 0.000 claims description 3
- 229910001309 Ferromolybdenum Inorganic materials 0.000 claims description 3
- 229910000592 Ferroniobium Inorganic materials 0.000 claims description 3
- 229910000519 Ferrosilicon Inorganic materials 0.000 claims description 3
- 229910001200 Ferrotitanium Inorganic materials 0.000 claims description 3
- 229910000720 Silicomanganese Inorganic materials 0.000 claims description 3
- 229910052791 calcium Inorganic materials 0.000 claims description 3
- 239000011575 calcium Substances 0.000 claims description 3
- 238000009826 distribution Methods 0.000 claims description 3
- ZFGFKQDDQUAJQP-UHFFFAOYSA-N iron niobium Chemical compound [Fe].[Fe].[Nb] ZFGFKQDDQUAJQP-UHFFFAOYSA-N 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000005070 sampling Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 claims description 3
- 238000002844 melting Methods 0.000 abstract 1
- 230000008018 melting Effects 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 229910052750 molybdenum Inorganic materials 0.000 description 7
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 5
- 239000011733 molybdenum Substances 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 238000003723 Smelting Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910003296 Ni-Mo Inorganic materials 0.000 description 2
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000002161 passivation Methods 0.000 description 2
- 238000000682 scanning probe acoustic microscopy Methods 0.000 description 2
- 229910000599 Cr alloy Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000788 chromium alloy Substances 0.000 description 1
- VNTLIPZTSJSULJ-UHFFFAOYSA-N chromium molybdenum Chemical compound [Cr].[Mo] VNTLIPZTSJSULJ-UHFFFAOYSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/001—Continuous casting of metals, i.e. casting in indefinite lengths of specific alloys
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/0006—Adding metallic additives
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/0075—Treating in a ladle furnace, e.g. up-/reheating of molten steel within the ladle
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/06—Deoxidising, e.g. killing
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C33/00—Making ferrous alloys
- C22C33/04—Making ferrous alloys by melting
- C22C33/06—Making ferrous alloys by melting using master alloys
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/02—Ferrous alloys, e.g. steel alloys containing silicon
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/04—Ferrous alloys, e.g. steel alloys containing manganese
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/06—Ferrous alloys, e.g. steel alloys containing aluminium
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/18—Ferrous alloys, e.g. steel alloys containing chromium
- C22C38/22—Ferrous alloys, e.g. steel alloys containing chromium with molybdenum or tungsten
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/18—Ferrous alloys, e.g. steel alloys containing chromium
- C22C38/28—Ferrous alloys, e.g. steel alloys containing chromium with titanium or zirconium
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
The invention discloses a method for producing high-chromium corrosion-resistant sucker rod steel by a converter, which is mainly applied to a steel mill for producing the high-chromium corrosion-resistant sucker rod steel by utilizing a converter-LF refining furnace-continuous casting process flow. The chromium content of the high-chromium corrosion-resistant sucker rod is more than 5%. The chromium content cannot be directly added to the component requirement range in the LF furnace by adopting the traditional converter-LF refining furnace-continuous casting process flow. The method comprises the steps of adding most of ferrochrome into a converter through a high-level bin before tapping at the end point of the converter, melting alloy by means of heat of the converter, controlling chromium content of molten steel in the converter to be more than 4%, controlling chromium oxidation in the converter by means of a technical means, ensuring that the yield of chromium in the converter is more than 90%, greatly relieving temperature reduction caused by adding chromium components in a converter tapping deoxidization alloying process and an LF refining furnace, and finally obtaining specified components and proper casting temperature of the high-chromium corrosion-resistant sucker rod steel.
Description
Technical Field
The invention relates to a method for producing high-chromium corrosion-resistant sucker rod steel by a converter.
Background
In the traditional steelmaking process, chromium alloy is generally added in the tapping process of a converter, and component fine adjustment is carried out in the LF furnace process. According to the actual production on site, the temperature of molten steel is reduced to 8-10 ℃ every 1t of ferrochrome is added in the tapping process. According to the temperature drop range, for example, when smelting high-chromium corrosion-resistant sucker rod steel, the ferrochrome added in the tapping process of the converter is more than 10t, and the ferrochrome cannot be alloyed by adopting the conventional tapping process. Therefore, domestic manufacturers adopt intermediate frequency furnaces for smelting production. Under the condition of no intermediate frequency furnace and other alloy heating means, through experiments, the waste molten iron steel ratio can be adjusted through a converter, when the temperature before tapping at the smelting end reaches 1710-1720 ℃, most of ferrochrome is added into the converter through a high-level bin, the ferrochrome is melted by using the heat of the converter, a small amount of ferrochrome is continuously added in the tapping process for alloying, and the LF refining process continuously finely adjusts the components, so that the target components of the high-chromium corrosion-resistant sucker rod steel are finally met.
The primary form of sucker rod corrosion is cavitation. When the vapor pressure of the liquid is higher than its pressure with the surface of the sucker rod, bubbles will form near the surface of the sucker rod. In addition, gas dissolved in the liquid may be precipitated to generate bubbles. Then, when the bubbles flow to a place where the bubble pressure is lower than the liquid pressure, they are broken, and a large impact force is generated between the breaking moments. The sucker rod surface is repeatedly subjected to the repeated action of the instant impact force, and the surface material can fall off due to fatigue, so that small pits appear on the surface, the sucker rod surface is even further developed into a honeycomb shape, and large pits can be formed on the surface if the sucker rod surface is serious, and the depth can reach more than 3 mm. In the middle and later stages of the development of the oil field, along with the increase of the water content of the produced fluid, various ions are enriched around the sucker rod under the working condition, and when the sucker rod contacts with some corrosive ions or gaseous media, corrosion can occur, so that corrosion fatigue failure is most likely to occur.
Chromium-molybdenum steel is mostly adopted as steel for sucker rods, because chromium and molybdenum are surface active elements, the steel can block the anode process and promote the cathode process, and is beneficial to improving the corrosion resistance. When the sucker rod is in oil well operation, the sucker rod is mainly subjected to corrosion fatigue. A great deal of practical experience shows that the fatigue fracture failure of the sucker rod is mostly caused by pitting of the surface of the sucker rod. Pitting is a severe localized corrosion phenomenon that occurs in sucker rods in well fluid media. Therefore, the corrosion fatigue performance of the sucker rod must be improved, and the pitting corrosion resistance of the sucker rod must be improved. The results of studies on the pitting resistance of the alloy element show that the most effective elements for improving the pitting resistance of the steel are chromium and molybdenum. The study of the potential-pH diagram of Fe-Cr-Mo and Fe-Cr-Ni-Mo alloy experiments shows that chromium and molybdenum can reduce the ability of pitting nucleation and the growth rate of pitting development. Moreover, the effect of these two elements is also related to the nickel content in the steel. According to the analysis results of Auger Electron Spectroscopy (AES) and X-ray photoelectron spectroscopy (XPS) of the surface films of Fe-Cr-Mo and Fe-Cr-Ni-Mo alloys, the combined action of the 3 elements can increase the enrichment degree of chromium in the outer layer of the passivation film along with the increase of the contents of chromium, nickel and molybdenum, so that an outer layer film with better protectiveness is formed. Meanwhile, the molybdenum can also effectively inhibit the depletion of chromium in the transition layer between the outermost layer of the passivation film and the matrix metal, so that the repassivation capability is improved, and the corrosion resistance of the material is improved.
Disclosure of Invention
The invention aims to provide a method for producing high-chromium corrosion-resistant sucker rod steel by a converter, which has simple and reasonable production process, and continuously fine-adjusts components through an LF refining procedure, so as to finally meet target components of the high-chromium corrosion-resistant sucker rod steel.
The technical proposal adopted by the invention is that a method for producing high-chromium corrosion-resistant sucker rod steel by a converter,
and (3) designing components of the high-chromium corrosion-resistant sucker rod:
the process flow comprises the following steps: BOF-LF-CC;
alloying and adding modes of ferrochrome:
control of the converter end point: the converter adopts a supplementary blowing operation, the temperature of primary furnace pouring is 1660-1680 ℃, primary carbon pouring is 0.06-0.08%, the final tapping temperature after secondary supplementary blowing is 1710-1720 ℃, the final tapping carbon content is 0.03-0.05%, most ferrochrome is added into the converter through a high-level bin of the converter before final tapping, the chromium content of molten steel in the converter is controlled to be more than 4%, and the tapping temperature is 1620-1650 ℃;
deoxidizing and alloying control of converter tapping: the converter tapping process is added in sequence: 2kg/t of calcium carbide, silicomanganese, ferrosilicon and low-carbon ferrochromium; the ladle composition is controlled as follows:
LF refining process control: the converter reaches the temperature requirement of an LF furnace: 1540-1580 ℃, and controlling the slag alkalinity to be 2.8-3.2; alloy fine tuning: the fine adjustment of the steel ladle [ Cr ] adopts low-carbon ferrochrome, an LF furnace starts argon after molten steel arrives at a station according to the sampling result of a CAS procedure, 275kg of ferromolybdenum is added, low-carbon ferrochrome and ferroniobium alloy are added, and ferrotitanium is strictly forbidden to be added 20min before steel feeding; wire feeding control: taking possible aluminum components brought by the alloy into consideration, feeding wires according to the content of Al in the steel ladle, and controlling the ratio of calcium to aluminum in the molten steel according to 0.1-0.2; soft blowing time control: the soft blowing time is more than or equal to 16min;
and (3) controlling the components of a finished product:
and (3) process control of continuous casting procedures: the long water gap of the large ladle adopts argon seal protection, the argon flow is controlled at 50 m/h, the tundish is protected by a covering agent, the liquid level of the continuous casting tundish is continuously blown with argon, the argon blowing time of the tundish is ensured to be more than or equal to 5min before starting up, the sealing gasket is added to the immersed water gap, and the thickness of the casting powder and the casting powder added to the crystallizer is controlled at 40+/-5 mm; the covering slag uses peritectic steel covering slag, and the covering agent adopts a low-carbon covering agent; the cooling water flow of the crystallizer is controlled to be 115-125 m/h, and the specific water flow of secondary cooling water distribution is controlled to be 0.45-0.55L/Kg; adopting crystallizer electromagnetic stirring and terminal electromagnetic stirring;
the crystallizer and end electromagnetic stirring parameters are given in the following table:
the pulling speed is controlled to be less than or equal to 2.2m/min, and the lowest pulling speed is controlled to be 1.4m/min.
The invention is applied to the production of high-chromium steel by adopting a converter-LF refining furnace-continuous casting process flow, and has ideal cost control and product quality.
Description of the embodiments
A method for producing high-chromium corrosion-resistant sucker rod steel by a converter,
and (3) designing components of the high-chromium corrosion-resistant sucker rod:
the process flow comprises the following steps: BOF-LF-CC;
alloying and adding modes of ferrochrome:
control of the converter end point: the converter adopts a supplementary blowing operation, the temperature of primary furnace pouring is 1660-1680 ℃, primary carbon pouring is 0.06-0.08%, the final tapping temperature after secondary supplementary blowing is 1710-1720 ℃, the final tapping carbon content is 0.03-0.05%, most ferrochrome is added into the converter through a high-level bin of the converter before final tapping, the chromium content of molten steel in the converter is controlled to be more than 4%, and the tapping temperature is 1620-1650 ℃;
deoxidizing and alloying control of converter tapping: the converter tapping process is added in sequence: 2kg/t of calcium carbide, silicomanganese, ferrosilicon and low-carbon ferrochromium; the ladle composition is controlled as follows:
LF refining process control: the converter reaches the temperature requirement of an LF furnace: 1540-1580 ℃, and controlling the slag alkalinity to be 2.8-3.2; alloy fine tuning: the fine adjustment of the steel ladle [ Cr ] adopts low-carbon ferrochrome, an LF furnace starts argon after molten steel arrives at a station according to the sampling result of a CAS procedure, 275kg of ferromolybdenum is added, low-carbon ferrochrome and ferroniobium alloy are added, and ferrotitanium is strictly forbidden to be added 20min before steel feeding; wire feeding control: taking possible aluminum components brought by the alloy into consideration, feeding wires according to the content of Al in the steel ladle, and controlling the ratio of calcium to aluminum in the molten steel according to 0.1-0.2; soft blowing time control: the soft blowing time is more than or equal to 16min;
and (3) controlling the components of a finished product:
and (3) process control of continuous casting procedures: the long water gap of the large ladle adopts argon seal protection, the argon flow is controlled at 50 m/h, the tundish is protected by a covering agent, the liquid level of the continuous casting tundish is continuously blown with argon, the argon blowing time of the tundish is ensured to be more than or equal to 5min before starting up, the sealing gasket is added to the immersed water gap, and the thickness of the casting powder and the casting powder added to the crystallizer is controlled at 40+/-5 mm; the covering slag uses peritectic steel covering slag, and the covering agent adopts a low-carbon covering agent; the cooling water flow of the crystallizer is controlled to be 115-125 m/h, and the specific water flow of secondary cooling water distribution is controlled to be 0.45-0.55L/Kg; adopting crystallizer electromagnetic stirring and terminal electromagnetic stirring;
the crystallizer and end electromagnetic stirring parameters are given in the following table:
the pulling speed is controlled to be less than or equal to 2.2m/min, and the lowest pulling speed is controlled to be 1.4m/min.
Claims (1)
1. A method for producing high-chromium corrosion-resistant sucker rod steel by a converter is characterized by comprising the following steps:
and (3) designing components of the high-chromium corrosion-resistant sucker rod:
the process flow comprises the following steps: BOF-LF-CC;
alloying and adding modes of ferrochrome:
control of the converter end point: the converter adopts a supplementary blowing operation, the temperature of primary furnace pouring is 1660-1680 ℃, primary carbon pouring is 0.06-0.08%, the final tapping temperature after secondary supplementary blowing is 1710-1720 ℃, the final tapping carbon content is 0.03-0.05%, most ferrochrome is added into the converter through a high-level bin of the converter before final tapping, the chromium content of molten steel in the converter is controlled to be more than 4%, and the tapping temperature is 1620-1650 ℃;
deoxidizing and alloying control of converter tapping: the converter tapping process is added in sequence: 2kg/t of calcium carbide, silicomanganese, ferrosilicon and low-carbon ferrochromium; the ladle composition is controlled as follows:
LF refining process control: the converter reaches the temperature requirement of an LF furnace: 1540-1580 ℃, and controlling the slag alkalinity to be 2.8-3.2; alloy fine tuning: the fine adjustment of the steel ladle [ Cr ] adopts low-carbon ferrochrome, an LF furnace starts argon after molten steel arrives at a station according to the sampling result of a CAS procedure, 275kg of ferromolybdenum is added, low-carbon ferrochrome and ferroniobium alloy are added, and ferrotitanium is strictly forbidden to be added 20min before steel feeding; wire feeding control: taking possible aluminum components brought by the alloy into consideration, feeding wires according to the content of Al in the steel ladle, and controlling the ratio of calcium to aluminum in the molten steel according to 0.1-0.2; soft blowing time control: the soft blowing time is more than or equal to 16min;
and (3) controlling the components of a finished product:
and (3) process control of continuous casting procedures: the long water gap of the large ladle adopts argon seal protection, the argon flow is controlled at 50 m/h, the tundish is protected by a covering agent, the liquid level of the continuous casting tundish is continuously blown with argon, the argon blowing time of the tundish is ensured to be more than or equal to 5min before starting up, the sealing gasket is added to the immersed water gap, and the thickness of the casting powder and the casting powder added to the crystallizer is controlled at 40+/-5 mm; the covering slag uses peritectic steel covering slag, and the covering agent adopts a low-carbon covering agent; the cooling water flow of the crystallizer is controlled to be 115-125 m/h, and the specific water flow of secondary cooling water distribution is controlled to be 0.45-0.55L/Kg; adopting crystallizer electromagnetic stirring and terminal electromagnetic stirring;
the crystallizer and end electromagnetic stirring parameters are given in the following table:
the pulling speed is controlled to be less than or equal to 2.2m/min, and the lowest pulling speed is controlled to be 1.4m/min.
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101254527A (en) * | 2008-02-01 | 2008-09-03 | 湖南华菱涟源钢铁有限公司 | Method for producing low-carbon bainite high-strength steel based on thin slab continuous casting and rolling process |
CN114438397A (en) * | 2022-02-08 | 2022-05-06 | 新疆八一钢铁股份有限公司 | Production process of high-chromium corrosion-resistant sucker rod |
US20240068064A1 (en) * | 2021-01-15 | 2024-02-29 | Institute Of Research Of Iron And Steel, Jiangsu Province/Sha-Steel, Co. Ltd (CN) | 400 MPa CORROSION-RESISTANT STEEL BAR AND PRODUCTION METHOD THEREOF |
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