CN117947331A - Preparation method of super duplex stainless steel plate blank electrode - Google Patents

Preparation method of super duplex stainless steel plate blank electrode Download PDF

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Publication number
CN117947331A
CN117947331A CN202410262589.6A CN202410262589A CN117947331A CN 117947331 A CN117947331 A CN 117947331A CN 202410262589 A CN202410262589 A CN 202410262589A CN 117947331 A CN117947331 A CN 117947331A
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CN
China
Prior art keywords
stainless steel
duplex stainless
super duplex
furnace
smelting
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CN202410262589.6A
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Chinese (zh)
Inventor
李宇宙
罗利阳
李珂
朱珍彪
刘军
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711th Research Institute of CSIC
China State Shipbuilding Corp Ltd
CSSC Shuangrui Luoyang Special Equipment Co Ltd
Original Assignee
711th Research Institute of CSIC
China State Shipbuilding Corp Ltd
CSSC Shuangrui Luoyang Special Equipment Co Ltd
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Application filed by 711th Research Institute of CSIC, China State Shipbuilding Corp Ltd, CSSC Shuangrui Luoyang Special Equipment Co Ltd filed Critical 711th Research Institute of CSIC
Priority to CN202410262589.6A priority Critical patent/CN117947331A/en
Publication of CN117947331A publication Critical patent/CN117947331A/en
Pending legal-status Critical Current

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Abstract

The embodiment of the invention provides a preparation method of a super duplex stainless steel plate blank electrode. The method adopts a process route of medium frequency furnace smelting, AOD furnace refining and sand box die casting. The invention adopts the technological route of intermediate frequency furnace smelting, AOD refining and sand box casting and finally heat treatment through electrode smelting control of the super duplex stainless steel plate blank. Not only meets the requirement of too narrow component range of the consumable electrode part of the dual-phase steel, but also ensures that the material has higher cleanliness and component uniformity, and controls the precipitation of the intermediate phase of the stainless steel.

Description

Preparation method of super duplex stainless steel plate blank electrode
Technical Field
The application relates to the technical field of stainless steel metallurgy, in particular to a preparation method of a super duplex stainless steel plate blank electrode.
Background
The duplex stainless steel is the stainless steel with the ferrite and the austenite accounting for about 50% of each structure, the excellent toughness and the weldability of the austenitic stainless steel are combined with the higher strength and the chloride stress corrosion resistance of the ferritic stainless steel, the advantages of the two are utilized to rapidly develop from the 90 th century, and the duplex stainless steel has been widely applied at home and abroad at present.
The super duplex stainless steel is based on stainless steel, and has relatively high balance component design to the Cr, mo and N content in the steel while controlling the carbon content in relatively low level. The steel has high stress corrosion resistance, pore corrosion resistance and crevice corrosion resistance.
UNS S32750 is a super duplex stainless steel suitable for ASME standard and has the composition shown in table 1 below.
Table 1 UNS s32750 standard composition (wt%) currently consumable electrode production most use vacuum consumable furnace/electric furnace smelting, LF refining, VD vacuum degassing casting process routes. The route has a more severe equipment requirement, and the production electrode can not flexibly adjust the specification according to the requirement due to vacuum casting, so that the operation is complex.
Disclosure of Invention
The embodiment of the invention provides a preparation method of a super duplex stainless steel plate blank electrode, which comprises the following steps: intermediate frequency furnace smelting, argon oxygen decarburization AOD furnace refining and sand box die casting.
In some embodiments, the intermediate frequency furnace smelting comprises:
Pre-starting the slag charge bedding before smelting, wherein the smelting process is started at 50% power, and sequentially adding pure iron, furnace return materials, tungsten bars, electrolytic nickel, molybdenum bars, metallic chromium and chromium nitride iron;
After slag skimming is finished, new slag is additionally manufactured to prevent P from returning, and the added slag comprises lime and fluorite, so that the fluidity of furnace burden is ensured. In some embodiments, the AOD furnace refining includes:
Oxygen blowing and decarburization are carried out in the oxidation period of the dual-phase steel until the content of N is controlled below 0.02%, the content of Mn and Cr is controlled at the upper limit, and the content of C is controlled by deoxidizing crystalline Si in the reduction period.
In some embodiments, the flask molding includes:
And (3) casting by a bottom pouring method, wherein a sand box is added with a riser to improve a solidification structure, the amount of riser steel water is more than 30% of the casting weight, and the casting is free of center looseness and shrinkage cavity.
In some embodiments, the flask molding further comprises:
The sand box is uniformly provided with air outlet holes so as to reduce the pressure applied to the primary shell.
The electrode prepared by the method provided by the embodiment of the invention has good surface quality, and no obvious air holes are formed on the polished surface after heat treatment. The chemical components are qualified, and the PRE value requirement is met. The interior of the material has no obvious segregation, looseness, shrinkage cavity, obvious bubbles, cracks and the like, and various inclusions meet the requirements.
The electrode raw materials prepared by the method of the embodiment of the invention are scrap steel and various alloys, slag formers and deoxidizers, and compared with the corrosion-resistant alloy with the same level, nitrogen is used for replacing part of nickel, molybdenum and the like, so that the production cost is reduced; meanwhile, in the casting process, the ways of covering slag, low superheat degree and the like are adopted, so that the solid solution effect of nitrogen in molten steel is ensured, and escape is reduced.
Detailed Description
In order to more fully understand the features and technical content of the embodiments of the present application, the implementation of the embodiments of the present application will be described in detail below, which is for reference only, but is not intended to limit the embodiments of the present application.
Besides providing an extra production route, the invention has simple equipment and more flexible casting specification, and reduces the smelting cost of electrode ton steel to 3000 yuan/ton.
The invention provides a preparation method of a super duplex stainless steel plate slab ingot-drawing electrode, wherein the nitrogen content of the electrode is higher than 0.3%, and the pitting corrosion equivalent is higher than 41. The invention comprises two aspects of design of internal control components and smelting process. The invention relates to a dual-phase stainless steel slab ingot stripping electrode, which is smelted by adopting a mode of a 3-ton medium-frequency induction furnace, a 3-ton argon oxygen decarburization (argon oxygen decarburizationfurnace, AOD) furnace and die casting.
The properties of duplex stainless steel are affected by the ratio of the two phases. The most important factor affecting corrosion resistance is the balance ratio of austenite and ferrite.
The influencing factors influencing the phase ratio of the duplex stainless steel include two, namely the composition of the duplex stainless steel, which has a decisive effect on the phase ratio, and the solution temperature of the duplex stainless steel. Therefore, during smelting of the duplex stainless steel, the internal control components must be designed, the ferrite content is ensured to be controlled to be 50%, and the designed internal control components are shown in table 2.
TABLE 2 control composition (wt%) in duplex stainless steel SAF 2507
The carbon content is controlled below 0.02%, which is beneficial to improving corrosion resistance, and the sensitization problem of the steel is negligible due to the low carbon content and the existence of ferrite phase. Si content is too high to be detrimental to the thermoplasticity, and Si as a ferrite forming element can significantly raise the precipitation temperature and precipitation rate of a part of unstable phases, and can promote the phase equilibrium temperature to move toward a lower temperature direction, approaching the precipitation temperature of the precipitated phases, so that the control is required to be at a lower level. Although the Mn content has little influence on precipitation and the like, grain boundary segregation is liable to occur, but a certain Mn content is required to ensure the solubility of N. Cr and N are controlled at the upper limit, so that the corrosion resistance of the material can be ensured, and the maximum harmful phase sigma phase precipitation temperature of the material is the lowest; the Ni element belongs to an austenite forming element, and increases the phase equilibrium temperature of the material, and as Ni increases, the precipitation temperature and precipitation rate of a part of the precipitated phase are greatly reduced, preferably at the middle and lower limits. Mo is controlled at the upper limit, which is favorable for keeping the ferrite content stable and ensuring the corrosion resistance of the material. The N content is controlled at the upper limit, so that the cavitation erosion resistance of the material can be improved, the balance stability of a two-phase structure can be maintained at high temperature, and the stability is of great significance to welding. The internal control component standard of P and S is stricter, and the material performance is ensured. O is controlled at a lower level, which is beneficial to ensuring the cleanliness and inclusion level of the material.
(1) Preparing steelmaking raw materials.
Alloy furnace burden: pure iron, scrap steel, high nitrogen ferrochrome, nickel plates, ferromolybdenum and chromium nitride; slag former and deoxidizer: active lime, fluorite, crystalline silicon and aluminum ingot.
The alloy furnace burden, the slag former and the deoxidizer should be ensured to be clean and free of greasy dirt and the like before smelting, baked and kept clean and dry.
(2) Intermediate frequency induction furnace smelting
To ensure the drying of the neutral furnace lining of the intermediate frequency furnace and to purify the molten steel. Before smelting, active lime and fluorite are put into a furnace to slag (accounting for 1% -1.5% of the total molten steel). Adding scrap steel, ferrochrome, nickel plate and ferromolybdenum. The power of the intermediate frequency furnace is just set to be 50% of the total power at the beginning of the power supply, the duration is about 10 minutes, and the power is gradually adjusted to be maximum after the induction preheating of the furnace body is stable.
After smelting, along with melting of materials in the bottom of the furnace, the materials need to be rammed in time to prevent bridging, and meanwhile pure iron, scrap steel, nickel plates, ferromolybdenum and chromium nitride are added. After furnace burden is melted down, taking molten steel by a quartz tube, performing air cooling solidification to obtain a spectrum sample, performing smelting analysis, if the components are proper, then adjusting the power of an intermediate frequency furnace to about 50%, transferring the molten steel into a ladle baked in advance, and rapidly adding the molten steel into an AOD furnace for refining in order to ensure the temperature of the molten steel.
(3) Refining in AOD furnace
The AOD furnace has the greatest effect of oxygen blowing, decarburization and chromium retention, and can be divided into four stages of oxygen blowing, reduction, component adjustment and tapping. Adding lime and magnesia into the molten steel after adding into a furnace to perform slag formation, then blowing oxygen, performing decarburization, and performing sampling analysis by using the same method when the decarburization degree is less than 0.02% of the required degree; in the reduction stage, in order to ensure that the carbon content is not increased again, reducing by using elemental crystalline silicon, simultaneously blowing argon to stir, and after the reduction is finished, taking a spectrum sample and a gas sample for component analysis; in the component adjustment stage, the component adjustment is carried out,
According to the spectrum result, chromium nitride, electrolytic nickel and the like can be added into the AOD furnace to carry out component fine adjustment to target internal control components; after the component adjustment is finished, a small amount of aluminum ingot (about 20 Kg) is added for Wen Zhenjing to ensure the casting temperature (1550+/-10 ℃) after the protection of the covering agent is added to the surface of the molten steel, and casting is carried out after about 3 minutes.
(4) Electrode treatment
During the cooling process of the sand box, the cast electrode can generate metal intermediate phases and inclusions such as carbide, nitride and the like, and the precipitation of the metal intermediate phases and the inclusions can adversely affect the plasticity, toughness and corrosion resistance of the electrode. In order to ensure the subsequent processing and grinding of the electrode, the electrode needs to be subjected to solution heat treatment. The solid solution temperature was set to 1120 (+ -20) deg.C, and water-cooled.
The technical schemes described in the embodiments of the present application may be arbitrarily combined without any collision.
The foregoing is merely illustrative of the present application, and the present application is not limited thereto, and any person skilled in the art will readily recognize that variations or substitutions are within the scope of the present application. Therefore, the protection scope of the present application shall be subject to the protection scope of the claims.

Claims (5)

1. A method for preparing a super duplex stainless steel plate blank electrode, which is characterized by comprising the following steps: intermediate frequency furnace smelting, argon oxygen decarburization AOD furnace refining and sand box die casting.
2. The method for preparing the super duplex stainless steel slab electrode according to claim 1, wherein the intermediate frequency furnace smelting comprises:
Pre-starting the slag charge bedding before smelting, wherein the smelting process is started at 50% power, and sequentially adding pure iron, furnace return materials, tungsten bars, electrolytic nickel, molybdenum bars, metallic chromium and chromium nitride iron;
after slag skimming is finished, new slag is additionally manufactured to prevent P from returning, and the added slag comprises lime and fluorite, so that the fluidity of furnace burden is ensured.
3. The method for preparing a super duplex stainless steel slab electrode according to claim 1, wherein the AOD furnace refining comprises:
Oxygen blowing and decarburization are carried out in the oxidation period of the dual-phase steel until the content of N is controlled below 0.02%, the content of Mn and Cr is controlled at the upper limit, and the content of C is controlled by deoxidizing crystalline Si in the reduction period.
4. The method of preparing a super duplex stainless steel slab electrode according to claim 1, wherein the flask molding comprises:
And (3) casting by a bottom pouring method, wherein a sand box is added with a riser to improve a solidification structure, the amount of riser steel water is more than 30% of the casting weight, and the casting is free of center looseness and shrinkage cavity.
5. The method of preparing a super duplex stainless steel slab electrode according to claim 4, wherein the flask molding further comprises:
The sand box is uniformly provided with air outlet holes so as to reduce the pressure applied to the primary shell.
CN202410262589.6A 2024-03-07 2024-03-07 Preparation method of super duplex stainless steel plate blank electrode Pending CN117947331A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202410262589.6A CN117947331A (en) 2024-03-07 2024-03-07 Preparation method of super duplex stainless steel plate blank electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202410262589.6A CN117947331A (en) 2024-03-07 2024-03-07 Preparation method of super duplex stainless steel plate blank electrode

Publications (1)

Publication Number Publication Date
CN117947331A true CN117947331A (en) 2024-04-30

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202410262589.6A Pending CN117947331A (en) 2024-03-07 2024-03-07 Preparation method of super duplex stainless steel plate blank electrode

Country Status (1)

Country Link
CN (1) CN117947331A (en)

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