WO2022001874A1 - Slag-splashing fettling method - Google Patents
Slag-splashing fettling method Download PDFInfo
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- WO2022001874A1 WO2022001874A1 PCT/CN2021/102396 CN2021102396W WO2022001874A1 WO 2022001874 A1 WO2022001874 A1 WO 2022001874A1 CN 2021102396 W CN2021102396 W CN 2021102396W WO 2022001874 A1 WO2022001874 A1 WO 2022001874A1
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- WIPO (PCT)
- Prior art keywords
- slag
- converter
- splashing
- height
- furnace
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Classifications
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- 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
- C21C5/36—Processes yielding slags of special composition
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- 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
- C21C5/30—Regulating or controlling the blowing
- C21C5/34—Blowing through the bath
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- 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
- C21C5/42—Constructional features of converters
- C21C5/44—Refractory linings
-
- 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
- C21C5/42—Constructional features of converters
- C21C5/44—Refractory linings
- C21C5/441—Equipment used for making or repairing linings
- C21C5/443—Hot fettling; Flame gunning
Definitions
- the invention relates to an iron and steel smelting technology, in particular to a slag splashing and repairing method for furnace bottom maintenance.
- the furnace lining in the converter will be eroded to varying degrees due to the high temperature and high oxidizing environment in the converter hearth. Especially in the smelting process of low carbon steel, the erosion and damage of the furnace lining is more serious. If the height of the furnace lining at the bottom of the furnace decreases, the furnace age will be shortened. In addition, since the current converters all use top-bottom combined blowing, the bottom of the converter is provided with a bottom blowing gas supply element. Although the bottom blowing of the converter can effectively promote the stirring of the metal molten pool, the increase in the strength of the bottom blowing gas supply is conducive to improving the stirring.
- the Chinese patent discloses a method for controlling the exposure of the bottom blowing gun of the converter.
- the method adopts a large bottom blowing flow rate of 500-600 m 3 /h in the process of the converter tapping, and after the slag splashing operation is completed, the The bottom blowing flow rate of the bottom blowing gun is reduced to 150-200 m 3 /h, so that the mushroom head with low melting point can be formed above the bottom blowing gun.
- the mushroom head with low melting point above the bottom blow gun can be rapidly melted, so as to ensure that the bottom blow gun is exposed, improve the bottom blow effect, and reduce the carbon and oxygen accumulation at the end of the converter.
- Chinese patent application discloses a method of maintaining the converter bottom blowing tuyeres, the process is ended in the steel converter, down converter slag before, by bottom blowing converter element blown CH 4 mixed gas of nitrogen gas and ambient air to cool the slag .
- different cooling energy can be achieved under the same bottom blowing flow rate, and it can be adjusted according to the requirements of the converter tuyere maintenance process, so as to realize the control of furnace bottom gold. Effective control of the slag mushroom head, thus realizing the maintenance of the converter tuyere.
- inventive methods all propose methods for exposing and maintaining the bottom tuyere, but neither the bottom blowing air supply control process nor the bottom blowing vent maintenance can achieve both erosion maintenance and ventilation effects.
- the purpose of the present invention is to provide a slag splashing and furnace repairing method that is beneficial to the maintenance of the furnace bottom.
- the slag splashing and furnace repairing method of the present invention improves the slag splashing and furnace repairing process, and adopts the converter slag splashing and furnace repairing that matches the production rhythm of the converter.
- the technology improves the bottom blowing efficiency of the converter and prolongs the life of the bottom blowing port.
- a method for repairing furnace by splashing slag comprising:
- the slag splashing process shall be used to perform the slag splashing operation on the converter.
- the air supply flow rate is 1000Nm 3 /h ⁇ 1600Nm 3 /h (standard cubic meters per hour), and is gradually adjusted within the above interval with time.
- the slag splashing process shall be used to carry out the slag splashing operation on the converter.
- the bottom blowing gas supply is implemented to the converter, and the gas supply flow rate is 400Nm 3 /h ⁇ 1200Nm 3 /h, and is gradually adjusted within the above interval with time.
- the converter After each tap of the converter is finished, if the eroded height of the bottom lining of the converter exceeds the second erosion height, the converter shall be repaired by the fast repairing process of the repairing material. During the repairing operation, the converter shall be repaired. Bottom blowing air supply, the air supply flow rate is 400Nm 3 /h ⁇ 1600Nm 3 /h, and is gradually adjusted within the above interval with time.
- H represents the reference zero position (the thickness of the furnace bottom, mm)
- H 0 represents the original furnace bottom thickness (mm)
- a is the coefficient (value range 0.06 ⁇ 0.08)
- L is the furnace age (value range 1 ⁇ 10000 , times; if the actual furnace age exceeds 10,000 times, it will be calculated as 10,000 times).
- the slag splashing repairing method further includes: when the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, after the slag splashing process is used to perform the slag splashing operation on the converter, It is judged whether there is a depression at the bottom air outlet. If there is a depression, the converter is repaired by the fast charging process of the charging material. If there is no depression, the converter is repaired by the slag repairing process.
- the slag repairing process includes: after the slag splashing operation is completed, the slag hanging operation of the shaking furnace is performed; after the slag hanging operation of the shaking furnace is completed, the slag cooling and repairing operation of the converter is performed after a period of standing time.
- the slag hanging operation of the shaking furnace refers to: by rotating the converter to the charging side and the tapping side, the molten slag is coated on the furnace bottom during the rotation process to achieve the purpose of uniformly increasing the thickness of the furnace bottom; the slag cooling and repairing operation refers to : Through slag cooling, the molten slag becomes solid slag and condenses on the bottom of the furnace and does not flow to achieve the purpose of repairing the furnace.
- the slag adjustment and splashing process includes: judging whether the amount of slag after the converter is tapped is greater than 1/10 of the capacity of the converter; To the slag splashing gun position, the oxygen lance is used to blow nitrogen and slag splashing on the slag; after the nitrogen slag splashing operation starts, limestone is added first, and then nitrogen is blown; dolomite is added during the slag splashing operation, and the oxygen lance is controlled to implement the sliding gun operate.
- the quick repairing process of the charging material includes: pouring out all the slag, then adding the charging charging into the furnace, shaking the furnace after the charging charging is melted, and making the charging charging flow to the position where the charging is required.
- the charging material is a magnesium carbonaceous material with a mass percentage content of 75-77% of magnesium oxide and a particle size of 5-8 mm.
- the main components of the charging material are, for example, 75-77% by mass of magnesium oxide, 6-10% by mass of carbon, and a small amount of pitch and binder.
- the process of pouring slag first and then splashing slag includes: pouring out 1/3-1/2 of the amount of slag slag; lowering the height of the oxygen lance to the cooling lance position, and the oxygen lance performs a nitrogen blowing cooling operation on the slag; The height of the oxygen lance reaches the slag splashing lance position, and the oxygen lance performs nitrogen blowing and slag splashing operation on the slag.
- the first erosion height can be set in the range of 80-120 mm, and the second erosion height can be set in the range of 180-220 mm. Specifically, the first erosion height was 100 mm, and the second erosion height was 200 mm.
- the slag splashing repairing method when the eroded height of the bottom lining of the converter does not exceed the first erosion height, that is, in the initial stage of the converter furnace, the slag splashing process can be shortened by first pouring the slag and then splashing the slag.
- the retention time of slag in the converter is not long, and the time for erosion of the bottom air outlet and furnace lining of the converter is short, so that the bottom air vent and furnace bottom lining of the converter can be well maintained, and splashing can be reduced. Slag cost.
- the slag splashing repair method when the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, that is, in the middle stage of the converter furnace, the slag slag splashing process is adopted, and the slag splashing process is adopted.
- the content of MgO in the slag can reduce the erosion rate of the bottom air outlet and the bottom lining of the converter, and at the same time, it can also shorten the slag splashing time and improve the operating efficiency of the converter.
- the slag filling furnace process can also be used, and the slag slag after slag splashing has the characteristics of high MgO content.
- a layer of slag can be covered on the bottom air outlet and the furnace bottom lining, thereby slowing down the bottom air blowing of the converter.
- the furnace repairing process is adopted.
- the fluidity of the charging material is good, and the sintering speed is fast.
- the charging material to repair the furnace is fast, the repairing quality of the depression in the bottom of the furnace is high, and the corrosion resistance is good.
- the slag splashing and furnace repairing method provided by the present disclosure has the beneficial effects of shortening the slag splashing time by improving the slag splashing and furnace repairing processes.
- the converter slag splashing and repairing process matched with the production rhythm not only controls the erosion rate of the bottom lining and bottom blowing port of the converter, but also ensures the metallurgical effect of the bottom blowing port, thereby improving the bottom blowing efficiency of the converter and prolonging the bottom blowing rate.
- the life of the air outlet realizes the purpose of synchronizing the life of the bottom air outlet with the furnace age of the converter.
- This embodiment provides a slag splashing repairing method that is beneficial to furnace bottom maintenance.
- the implementation background of this embodiment is a converter steelmaking operation area of an iron and steel enterprise, and the slag splashing repairing method is implemented for a 300t converter in the operation area.
- the slag splashing repair method provided by the present disclosure is implemented on the converter.
- the slag splashing and furnace repairing method includes:
- the slag splashing operation is performed on the converter by the process of pouring slag first and then slag splashing. Bottom blowing air supply, the air supply flow is gradually adjusted over time.
- the slag splashing process is used to carry out the slag splashing operation on the converter.
- the bottom blowing gas supply is implemented to the converter, and the gas supply flow is gradually adjusted over time.
- the converter After the tapping of each heat of the converter, if the eroded height of the bottom lining of the converter exceeds the second erosion height, the converter shall be repaired by the fast repairing process with the repairing material. During the repairing process, the bottom of the converter shall be repaired. Blow air supply, and the air supply flow is gradually adjusted over time.
- bottom blowing gas supply is implemented to the converter, and the gas supply flow rate is gradually adjusted over time. Maintaining a certain bottom blowing flow rate can prevent the bottom blowing port from being blocked during the slag splashing repair process, and since the viscosity of the slag will change during the slag splash repairing process, the flow rate needs to be adjusted during the gas supply process. Generally speaking, the slag will become more viscous with time, so the bottom blowing flow is usually increased gradually with time; however, when the slag adjustment and slag splashing process is implemented, the heat of the slag is needed to melt the intermediate process of slag splashing.
- the first erosion height and the second erosion height can be adjusted according to the actual situation of the converter.
- the first erosion height and the second erosion height can be adjusted according to the actual situation of the converter.
- the first erosion height and the second erosion height can be reduced. If the converter age is greater than 8000 times, the first erosion height can be 80mm, and the second erosion height can be 180mm; if the converter age is less than 4000 times, the second erosion height
- the first erosion height may be 120mm, and the second erosion height may be 220mm.
- the first erosion height is preferably 100 mm
- the second erosion height is preferably 200 mm.
- the slag splashing repairing method further comprises: when the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, after the slag splashing operation is performed on the converter using the slag-adjusting and slag-splashing process, It is judged whether there is a depression at the bottom air outlet. If there is a depression, the converter is repaired by the fast charging process of the charging material. If there is no depression, the converter is repaired by the slag repairing process.
- the process of pouring the slag first and then splashing the slag includes: pouring out 1/3-1/2 of the amount of slag; lowering the height of the oxygen lance to the cooling lance position, and the oxygen lance performs a nitrogen blowing cooling operation on the slag; then, lowering the height of the oxygen lance To the slag splashing gun position, the oxygen lance performs nitrogen blowing and slag splashing operation on the slag.
- the slag adjusting and splashing process includes: judging whether the amount of slag is sufficient after the converter is tapped, and the basis for judging whether the amount of slag is sufficient is whether the amount of slag is greater than 1/10 of the capacity of the converter, and if so, first pour out 1/3 of the amount of slag ⁇ 1/2; then, lower the height of the oxygen lance to the slag splashing lance position, and the oxygen lance performs nitrogen blowing and slag splashing operation on the slag.
- the advantage of the slag adjustment and splashing process is that by adjusting the slag, the content of MgO in the slag is increased, the erosion rate of the air outlet at the bottom of the converter and the lining of the furnace bottom is reduced, and the slag splashing time is shortened and the operation efficiency of the converter is improved.
- the slag repairing process includes: after the slag splashing operation is completed, the shaking furnace slag hanging operation is performed; after the shaking furnace slag hanging operation is completed and a period of standing time is passed, the slag cooling and furnace repairing operation is performed.
- the advantage of the slag repair process is that the slag after slag splashing has a high content of MgO. After a period of standing time, a layer of slag can be covered on the bottom air vent and the furnace bottom lining to slow down the converter bottom air vent and furnace bottom refractories. erosion rate while maintaining the breathability of the bottom air vents.
- the rapid furnace repairing process of the charging material includes: pouring out all the slag; adding the charging charging material into the furnace, and shaking the furnace after the charging charging material is melted, so that the charging charging material flows to the position where the charging furnace is required.
- the advantages of the quick repairing process with the repairing charge are that the fluidity of the repairing charge is good and the sintering speed is fast, so the speed of repairing the furnace with the repairing charge is fast, the repair quality of the depression in the bottom of the furnace is high, and the corrosion resistance is good, which can slow down the bottom of the converter. Melting loss rate of blow vent and furnace bottom lining.
- the eroded height of the furnace bottom lining can actually reflect the degree of erosion of the bottom blowing port. That is to say, the maintenance objects targeted by the slag splashing and furnace repairing method in this embodiment include the furnace bottom and the bottom air outlet.
- the slag splashing and furnace repairing method of the present embodiment shortens the slag splashing time by improving the slag splashing and furnace repairing processes, and adopts the converter slag splashing and repairing methods that match the production rhythm of the converter according to the blowing port at the bottom of the converter and the erosion rate of the furnace bottom lining.
- the furnace process not only controls the erosion rate of the bottom lining of the converter and the bottom blowing port, but also ensures the metallurgical effect of the bottom blowing port, thereby improving the bottom blowing efficiency of the converter, prolonging the life of the bottom blowing port, and realizing the bottom blowing port.
- the converter is implemented with the slag splashing repair method of the present invention.
- the first erosion height is set to 100mm.
- the process of pouring slag first and then splashing slag is implemented.
- the implementation process is as follows:
- the converter implements bottom blowing air supply, and the air supply flow is gradually increased with time, specifically: 1200Nm 3 /h in the stage of 0-60 seconds; 1400Nm 3 /h in the stage of 60-120 seconds; 120 seconds 1600Nm 3 /h to the end stage.
- the converter is implemented with the slag splashing repair method of the present invention.
- the first erosion height is set to 100mm
- the second erosion height is set to 200mm.
- the eroded height of the converter bottom lining is greater than 100mm but less than 200mm, that is, the eroded height of the converter bottom lining exceeds the first erosion height but does not exceed the first erosion height.
- gas flow rate gradually adjusted over time, specifically: 0 to 30 seconds stage 1000Nm 3 / h; 30 ⁇ 120 seconds stage 800Nm 3 / h; 120 seconds
- the end stage is 1200Nm 3 /h.
- the bottom blowing air supply flow rate was reduced in the 30-120 second stage, in order to fully melt the dolomite added in this stage by using the heat of the slag. If the air supply flow rate is high, it is not conducive to the melting of the dolomite.
- the converter is implemented with the slag splashing repair method of the present invention.
- the first erosion height is set to 100mm
- the second erosion height is set to 200mm.
- the eroded height of the converter bottom lining is greater than 100mm but less than 200mm, that is, the eroded height of the converter bottom lining exceeds the first erosion height but does not exceed the first erosion height.
- the slag adjustment and slag splashing process is carried out and then the slag repair process is carried out.
- the implementation process is as follows:
- the converter implements bottom blowing and gas supply, and the gas supply flow rate is gradually adjusted over time, and the specific flow rate is the same as that in Example 2.
- the slag hanging operation of the shaking furnace is carried out, and the slag hanging back and forth of the shaking furnace is 1 to 3 times.
- the furnace is shaken to the zero position, and the slag cooling and furnace repairing operation is carried out after a period of 20-40 minutes of standing time.
- the converter continues to implement bottom blowing gas supply, and the gas supply flow rate is gradually increased with time.
- the specific flow rate is: 560Nm 3 /h in the stage of 0-5 minutes;
- the minute stage is 640Nm 3 /h;
- the 10-20 minute stage is 800Nm 3 /h;
- the 20-minute to end stage is 1000Nm 3 /h.
- the converter is implemented with the slag splashing repair method of the present invention.
- the second erosion height is set to 200mm.
- the fast-repairing process of the charging material is implemented. The implementation process is as follows:
- gas flow rate over time to gradually turn up specifically: Phase 0 to 5 minutes was 480Nm 3 / h; 5 ⁇ 10 minutes in a stepwise was 720Nm 3 / h; 10 ⁇ 20 minutes stage 800Nm 3 / h; 20 minutes to end phase of 1000Nm 3 / h.
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Abstract
Description
本发明涉及一种钢铁冶炼技术,尤其涉及一种利于炉底维护的溅渣补炉方法。The invention relates to an iron and steel smelting technology, in particular to a slag splashing and repairing method for furnace bottom maintenance.
在转炉炼钢过程中,由于转炉炉膛内是高温高氧化性环境,因此转炉内的炉衬会受到不同程度的侵蚀。尤其是在低碳钢冶炼过程中,炉衬的侵蚀损毁则更加严重,若炉底的炉衬高度下降,则会使炉龄缩短。此外,由于目前的转炉都是采用顶底复合吹的转炉,转炉底部设置有底吹供气元件,转炉底吹虽可有效促进金属熔池搅拌,底吹供气强度的增大有利于提高搅拌效果,但底吹供气强度增大的同时也会导致底吹风口及其周围护砖侵蚀加剧,因而也会导致炉龄缩短。因此,提升炉底炉衬及底吹风口的维护效果是延长炉龄的重要的途径。In the process of converter steelmaking, the furnace lining in the converter will be eroded to varying degrees due to the high temperature and high oxidizing environment in the converter hearth. Especially in the smelting process of low carbon steel, the erosion and damage of the furnace lining is more serious. If the height of the furnace lining at the bottom of the furnace decreases, the furnace age will be shortened. In addition, since the current converters all use top-bottom combined blowing, the bottom of the converter is provided with a bottom blowing gas supply element. Although the bottom blowing of the converter can effectively promote the stirring of the metal molten pool, the increase in the strength of the bottom blowing gas supply is conducive to improving the stirring. However, the increase in the strength of the bottom blowing air supply will also lead to aggravated erosion of the bottom blowing port and its surrounding bricks, which will also lead to a shortening of the furnace age. Therefore, improving the maintenance effect of the furnace bottom lining and the bottom air outlet is an important way to prolong the furnace life.
中国专利(CN106906329B)公开了一种控制转炉底吹枪裸露的方法,该方法在转炉出钢的过程中采用500~600m 3/h的大底吹流量,并且,在溅渣操作结束后,将底吹枪的底吹流量降至150~200m 3/h,从而能够在底吹枪上方形成低熔点的蘑菇头。采用该方法,在转炉吹炼前期,底吹枪上方的低熔点蘑菇头能够快速熔化,从而保证底吹枪裸露,提高了底吹效果,降低了转炉终点的碳氧积。 The Chinese patent (CN106906329B) discloses a method for controlling the exposure of the bottom blowing gun of the converter. The method adopts a large bottom blowing flow rate of 500-600 m 3 /h in the process of the converter tapping, and after the slag splashing operation is completed, the The bottom blowing flow rate of the bottom blowing gun is reduced to 150-200 m 3 /h, so that the mushroom head with low melting point can be formed above the bottom blowing gun. By adopting this method, in the early stage of converter blowing, the mushroom head with low melting point above the bottom blow gun can be rapidly melted, so as to ensure that the bottom blow gun is exposed, improve the bottom blow effect, and reduce the carbon and oxygen accumulation at the end of the converter.
中国专利申请(CN110863076A)公开了一种转炉底吹风口维护的方法,该方法是在转炉出钢结束、转炉倒渣之前,通过转炉底吹元件吹入CH 4和氮气混合气体来冷却风口周围炉渣。利用两种气体冷却能的不同,达到特定冷却能和供气强度,能够在相同的底吹流量条件下达到不同的冷却能,并能够依据转炉风口维护工艺的要求进行调节,实现对炉底金渣蘑菇头的有效控制,进而实现对转炉风口的维护。 Chinese patent application (CN110863076A) discloses a method of maintaining the converter bottom blowing tuyeres, the process is ended in the steel converter, down converter slag before, by bottom blowing converter element blown CH 4 mixed gas of nitrogen gas and ambient air to cool the slag . Using the difference in cooling energy of the two gases to achieve specific cooling energy and gas supply intensity, different cooling energy can be achieved under the same bottom blowing flow rate, and it can be adjusted according to the requirements of the converter tuyere maintenance process, so as to realize the control of furnace bottom gold. Effective control of the slag mushroom head, thus realizing the maintenance of the converter tuyere.
上述发明方法都提出了炉底风口裸露与维护的方法,但无论是从底吹供气控制工艺还是底吹风口维护的角度都不能使侵蚀维护与透气效果兼得。The above-mentioned inventive methods all propose methods for exposing and maintaining the bottom tuyere, but neither the bottom blowing air supply control process nor the bottom blowing vent maintenance can achieve both erosion maintenance and ventilation effects.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种利于炉底维护的溅渣补炉方法,本发明的溅渣补炉方法通过改进溅渣和补炉工艺,采用与转炉生产节奏相匹配的转炉溅渣和补炉工艺,提升了转炉底吹效率,延长了底吹风口的寿命。The purpose of the present invention is to provide a slag splashing and furnace repairing method that is beneficial to the maintenance of the furnace bottom. The slag splashing and furnace repairing method of the present invention improves the slag splashing and furnace repairing process, and adopts the converter slag splashing and furnace repairing that matches the production rhythm of the converter. The technology improves the bottom blowing efficiency of the converter and prolongs the life of the bottom blowing port.
为了实现上述技术目的,本发明采用如下技术方案:In order to realize above-mentioned technical purpose, the present invention adopts following technical scheme:
一种溅渣补炉方法,包括:A method for repairing furnace by splashing slag, comprising:
转炉每一炉出钢结束后,若转炉炉底炉衬被侵蚀高度未超过第一侵蚀高度,则采用先倒渣后溅渣工艺对转炉实施溅渣操作,在该溅渣过程中,对转炉实施底吹供气,供气流量为1000Nm 3/h~1600Nm 3/h(标立米每小时),并随时间在上述区间内逐步调整。 After each tap of the converter is completed, if the eroded height of the bottom lining of the converter does not exceed the first erosion height, the slag splashing process shall be used to perform the slag splashing operation on the converter. Bottom blowing air supply, the air supply flow rate is 1000Nm 3 /h ~ 1600Nm 3 /h (standard cubic meters per hour), and is gradually adjusted within the above interval with time.
转炉每一炉出钢结束后,若转炉炉底炉衬被侵蚀高度超过第一侵蚀高度但未超过第二侵蚀高度时,则采用调渣溅渣工艺对转炉实施溅渣操作,在该溅渣过程中,对转炉实施底吹供气,供气流量为400Nm 3/h~1200Nm 3/h,并随时间在上述区间内逐步调整。 After the tapping of each furnace of the converter, if the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, the slag splashing process shall be used to carry out the slag splashing operation on the converter. In the process, the bottom blowing gas supply is implemented to the converter, and the gas supply flow rate is 400Nm 3 /h~1200Nm 3 /h, and is gradually adjusted within the above interval with time.
转炉每一炉出钢结束后,若转炉炉底炉衬被侵蚀高度超过第二侵蚀高度时,则采用补炉料快补炉工艺对转炉实施补炉操作,在该补炉操作过程中,对转炉实施底吹供气,供气流量为400Nm 3/h~1600Nm 3/h,并随时间在上述区间内逐步调整。 After each tap of the converter is finished, if the eroded height of the bottom lining of the converter exceeds the second erosion height, the converter shall be repaired by the fast repairing process of the repairing material. During the repairing operation, the converter shall be repaired. Bottom blowing air supply, the air supply flow rate is 400Nm 3 /h ~ 1600Nm 3 /h, and is gradually adjusted within the above interval with time.
在上述技术方案中,侵蚀高度基准零位(炉底厚度)根据转炉炉龄变化,按照如下经验公式表示:H=H 0-a×L。式中,H表示基准零位(炉底厚度,mm),H 0表示原始炉底厚度(mm),a为系数(取值范围0.06~0.08),L为炉龄(取值范围1~10000,次数;如果实际炉龄超过10000次以后,则按10000次计算)。 In the above technical solution, the reference zero position of the erosion height (thickness of the furnace bottom) changes according to the age of the converter, and is expressed according to the following empirical formula: H=H 0 -a×L. In the formula, H represents the reference zero position (the thickness of the furnace bottom, mm), H 0 represents the original furnace bottom thickness (mm), a is the coefficient (value range 0.06~0.08), L is the furnace age (value range 1~10000 , times; if the actual furnace age exceeds 10,000 times, it will be calculated as 10,000 times).
进一步地,所述溅渣补炉方法还包括:当转炉炉底炉衬被侵蚀高度超过第一侵蚀高度但未超过第二侵蚀高度时,在采用调渣溅渣工艺对转炉实施溅渣操作后,判断底吹风口处是否有凹陷,若有凹陷,则采用补炉料快补炉工艺对转炉实施补炉操作,若无凹陷,则采用渣补炉工艺对转炉实施补炉操作。Further, the slag splashing repairing method further includes: when the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, after the slag splashing process is used to perform the slag splashing operation on the converter, It is judged whether there is a depression at the bottom air outlet. If there is a depression, the converter is repaired by the fast charging process of the charging material. If there is no depression, the converter is repaired by the slag repairing process.
具体地,所述渣补炉工艺包括:溅渣操作结束后实施摇炉挂渣操作;摇炉挂渣操作结束后,转炉经过一段静置时间后实施炉渣冷却补炉操作。其中,摇炉挂渣操作是指:通过向装入侧和出钢侧转动转炉,熔融炉渣在此转动过程中涂覆在炉底达到均匀增加炉底厚度的目的;炉渣冷却补炉操作是指:通过炉渣冷却,熔融状态的炉渣变为固态炉渣凝结在炉底不流动以达到补炉的目的。Specifically, the slag repairing process includes: after the slag splashing operation is completed, the slag hanging operation of the shaking furnace is performed; after the slag hanging operation of the shaking furnace is completed, the slag cooling and repairing operation of the converter is performed after a period of standing time. Among them, the slag hanging operation of the shaking furnace refers to: by rotating the converter to the charging side and the tapping side, the molten slag is coated on the furnace bottom during the rotation process to achieve the purpose of uniformly increasing the thickness of the furnace bottom; the slag cooling and repairing operation refers to : Through slag cooling, the molten slag becomes solid slag and condenses on the bottom of the furnace and does not flow to achieve the purpose of repairing the furnace.
具体地,所述调渣溅渣工艺包括:判断转炉出钢后炉渣量是否大于转炉容量 的1/10,若是,则先倒出炉渣渣量的1/3~1/2,降低氧枪高度至溅渣枪位,采用氧枪对炉渣实施吹氮气溅渣操作;吹氮气溅渣操作开始后先加入石灰石,随后再吹氮气;溅渣操作过程中加入白云石,并控制氧枪实施滑枪操作。Specifically, the slag adjustment and splashing process includes: judging whether the amount of slag after the converter is tapped is greater than 1/10 of the capacity of the converter; To the slag splashing gun position, the oxygen lance is used to blow nitrogen and slag splashing on the slag; after the nitrogen slag splashing operation starts, limestone is added first, and then nitrogen is blown; dolomite is added during the slag splashing operation, and the oxygen lance is controlled to implement the sliding gun operate.
具体地,所述补炉料快补炉工艺包括:倒掉全部炉渣,随后向炉内加入补炉料,待补炉料熔化后摇炉,使补炉料流淌至所需补炉的位置处。其中,补炉料是氧化镁质量百分含量为75~77%、粒度为5~8mm的镁碳质材料。补炉料主要成分例如为:氧化镁的质量百分含量75~77%,碳的质量百分含量6~10%,以及少量沥青和粘结剂。Specifically, the quick repairing process of the charging material includes: pouring out all the slag, then adding the charging charging into the furnace, shaking the furnace after the charging charging is melted, and making the charging charging flow to the position where the charging is required. Wherein, the charging material is a magnesium carbonaceous material with a mass percentage content of 75-77% of magnesium oxide and a particle size of 5-8 mm. The main components of the charging material are, for example, 75-77% by mass of magnesium oxide, 6-10% by mass of carbon, and a small amount of pitch and binder.
具体地,所述先倒渣后溅渣工艺包括:倒出炉渣渣量的1/3~1/2;降低氧枪高度至冷却枪位,氧枪对炉渣实施吹氮气冷却操作;随后,降低氧枪高度至溅渣枪位,氧枪对炉渣实施吹氮气溅渣操作。Specifically, the process of pouring slag first and then splashing slag includes: pouring out 1/3-1/2 of the amount of slag slag; lowering the height of the oxygen lance to the cooling lance position, and the oxygen lance performs a nitrogen blowing cooling operation on the slag; The height of the oxygen lance reaches the slag splashing lance position, and the oxygen lance performs nitrogen blowing and slag splashing operation on the slag.
进一步地,在容量为100~350t的转炉中,第一侵蚀高度可设置在80~120mm的范围内,第二侵蚀高度可设置在180~220mm的范围内。具体地,第一侵蚀高度为100mm,第二侵蚀高度为200mm。Further, in a converter with a capacity of 100-350t, the first erosion height can be set in the range of 80-120 mm, and the second erosion height can be set in the range of 180-220 mm. Specifically, the first erosion height was 100 mm, and the second erosion height was 200 mm.
在本公开提供的溅渣补炉方法中,当转炉炉底炉衬被侵蚀高度未超过第一侵蚀高度时,即在转炉炉役初期,采用先倒渣后溅渣工艺能够缩短溅渣时间。采用该工艺,炉渣在转炉内的留存时间不长,转炉底吹风口和炉底炉衬受侵蚀的时间则较短,从而能够对转炉底吹风口和炉底炉衬进行很好的维护,又降低溅渣成本。In the slag splashing repairing method provided by the present disclosure, when the eroded height of the bottom lining of the converter does not exceed the first erosion height, that is, in the initial stage of the converter furnace, the slag splashing process can be shortened by first pouring the slag and then splashing the slag. By adopting this process, the retention time of slag in the converter is not long, and the time for erosion of the bottom air outlet and furnace lining of the converter is short, so that the bottom air vent and furnace bottom lining of the converter can be well maintained, and splashing can be reduced. Slag cost.
在本公开提供的溅渣补炉方法中,当转炉炉底炉衬被侵蚀高度超过第一侵蚀高度但未超过第二侵蚀高度时,即在转炉炉役中期,采用调渣溅渣工艺,通过提高炉渣中MgO的含量来降低转炉底吹风口和炉底炉衬的侵蚀速度,同时还能缩短溅渣时间,提高转炉运行效率。进一步地,还可采用渣补炉工艺,利用溅渣后的炉渣MgO含量高的特点,通过一段静置时间后即可在底吹风口和炉底炉衬上覆盖一层炉渣,从而减缓转炉底吹风口和炉底耐材的侵蚀速度,同时保持底吹风口的透气性。In the slag splashing repair method provided by the present disclosure, when the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, that is, in the middle stage of the converter furnace, the slag slag splashing process is adopted, and the slag splashing process is adopted. The content of MgO in the slag can reduce the erosion rate of the bottom air outlet and the bottom lining of the converter, and at the same time, it can also shorten the slag splashing time and improve the operating efficiency of the converter. Further, the slag filling furnace process can also be used, and the slag slag after slag splashing has the characteristics of high MgO content. After a period of standing time, a layer of slag can be covered on the bottom air outlet and the furnace bottom lining, thereby slowing down the bottom air blowing of the converter. The erosion rate of the refractory material at the mouth and the bottom of the furnace, while maintaining the air permeability of the bottom air outlet.
在本公开提供的溅渣补炉方法中,当转炉炉底炉衬被侵蚀高度超过第二侵蚀高度时,即在转炉炉役后期,则采用补炉料快补炉工艺。补炉料的流动性好,且烧结速度快,用补炉料补炉,速度快、对炉底凹陷处的修补质量高、抗侵蚀性能好,可减缓转炉底吹风口和炉底炉衬的熔损速度。In the slag splashing repairing method provided by the present disclosure, when the eroded height of the bottom lining of the converter exceeds the second erosion height, that is, in the later stage of the converter's furnace operation, the furnace repairing process is adopted. The fluidity of the charging material is good, and the sintering speed is fast. Using the charging material to repair the furnace is fast, the repairing quality of the depression in the bottom of the furnace is high, and the corrosion resistance is good. .
本公开提供的溅渣补炉方法相对现有技术,其有益效果在于,通过改进溅渣 和补炉工艺,使溅渣时间缩短,并根据转炉底吹风口和炉底炉衬侵蚀速度,采用与转炉生产节奏相匹配的转炉溅渣和补炉工艺,既控制了转炉炉底炉衬和底吹风口的被侵蚀速度,又保证了底吹风口的冶金效果,从而提升了转炉底吹效率,延长了底吹风口的寿命,实现了底吹风口寿命与转炉炉龄同步的目的。Compared with the prior art, the slag splashing and furnace repairing method provided by the present disclosure has the beneficial effects of shortening the slag splashing time by improving the slag splashing and furnace repairing processes. The converter slag splashing and repairing process matched with the production rhythm not only controls the erosion rate of the bottom lining and bottom blowing port of the converter, but also ensures the metallurgical effect of the bottom blowing port, thereby improving the bottom blowing efficiency of the converter and prolonging the bottom blowing rate. The life of the air outlet realizes the purpose of synchronizing the life of the bottom air outlet with the furnace age of the converter.
下面通过具体实施例对本发明作进一步说明:The present invention is further described below by specific embodiment:
本实施方式提供了一种利于炉底维护的溅渣补炉方法,本实施方式的实施背景是某钢铁企业转炉炼钢作业区,所述溅渣补炉方法针对作业区内的300t转炉实施,通常来说,自转炉新炉役开始后,也就是新炉衬开炉后,每一炉出钢结束后均对转炉实施本公开提供的溅渣补炉方法。This embodiment provides a slag splashing repairing method that is beneficial to furnace bottom maintenance. The implementation background of this embodiment is a converter steelmaking operation area of an iron and steel enterprise, and the slag splashing repairing method is implemented for a 300t converter in the operation area. Generally speaking, after the new furnace operation of the converter is started, that is, after the new furnace lining is started, after the tapping of each furnace is completed, the slag splashing repair method provided by the present disclosure is implemented on the converter.
所述溅渣补炉方法包括:The slag splashing and furnace repairing method includes:
转炉每一炉出钢结束后,若转炉炉底炉衬被侵蚀高度未超过第一侵蚀高度时,采用先倒渣后溅渣工艺对转炉实施溅渣操作,在该溅渣过程中,对转炉实施底吹供气,供气流量随时间逐步调整。After each tap of the converter is completed, if the eroded height of the bottom lining of the converter does not exceed the first erosion height, the slag splashing operation is performed on the converter by the process of pouring slag first and then slag splashing. Bottom blowing air supply, the air supply flow is gradually adjusted over time.
转炉每一炉出钢结束后,若转炉炉底炉衬被侵蚀高度超过第一侵蚀高度但未超过第二侵蚀高度时,采用调渣溅渣工艺对转炉实施溅渣操作,在该溅渣过程中,对转炉实施底吹供气,供气流量随时间逐步调整。After the tapping of each furnace of the converter, if the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, the slag splashing process is used to carry out the slag splashing operation on the converter. During the slag splashing process , the bottom blowing gas supply is implemented to the converter, and the gas supply flow is gradually adjusted over time.
转炉每一炉出钢结束后,若转炉炉底炉衬被侵蚀高度超过第二侵蚀高度时,则采用补炉料快补炉工艺对转炉实施补炉操作,在该补炉过程中,对转炉实施底吹供气,供气流量随时间逐步调整。After the tapping of each heat of the converter, if the eroded height of the bottom lining of the converter exceeds the second erosion height, the converter shall be repaired by the fast repairing process with the repairing material. During the repairing process, the bottom of the converter shall be repaired. Blow air supply, and the air supply flow is gradually adjusted over time.
在本公开提供的溅渣补炉过程中,对转炉实施底吹供气,供气流量随时间逐步调整。保持一定的底吹流量能防止溅渣补炉过程中底吹风口堵塞,并且,由于溅渣补炉过程中炉渣的粘稠度会发生变化,因此需要在供气过程中对流量进行调整。通常来说,炉渣会随时间的延长而变得更加粘稠,因此,底吹流量通常是随时间逐步调大的;但实施调渣溅渣工艺时,需要炉渣的热量来熔化溅渣中间过程加入的白云石等调渣料,此时需要调小底吹供气流量,减少炉渣热量损失,便于白云石的熔化,随后再调大流量。在底吹供气的控制系统中,针对先倒渣后溅渣工艺、调渣溅渣工艺、渣补炉工艺和补炉料快补炉工艺均设置有自动控制模式,通过模式切换可实现底吹供气流量的自动控制调整。In the process of slag splashing and furnace repair provided by the present disclosure, bottom blowing gas supply is implemented to the converter, and the gas supply flow rate is gradually adjusted over time. Maintaining a certain bottom blowing flow rate can prevent the bottom blowing port from being blocked during the slag splashing repair process, and since the viscosity of the slag will change during the slag splash repairing process, the flow rate needs to be adjusted during the gas supply process. Generally speaking, the slag will become more viscous with time, so the bottom blowing flow is usually increased gradually with time; however, when the slag adjustment and slag splashing process is implemented, the heat of the slag is needed to melt the intermediate process of slag splashing. When adding dolomite and other slag-adjusting materials, it is necessary to adjust the bottom blowing air supply flow to reduce the heat loss of the slag and facilitate the melting of the dolomite, and then increase the flow. In the control system of bottom blowing gas supply, automatic control modes are set for the process of pouring slag first and then splashing slag, adjusting slag and splashing slag, repairing slag, and quickly repairing the furnace. Automatic control adjustment of air supply flow.
上述过程中,所述第一侵蚀高度和第二侵蚀高度可根据转炉实际情况作调整。一般来说,为了保持转炉炉衬侵蚀的均衡性,以及炉衬的使用安全,第一侵蚀高度和第二侵蚀高度可根据转炉实际情况作调整。需要长炉龄的转炉,第一侵蚀高度和第二侵蚀高度可减少,如转炉炉龄大于8000次,第一侵蚀高度可取80mm,第二侵蚀高度可取180mm;如转炉炉龄小于4000次,第一侵蚀高度可取120mm,第二侵蚀高度可取220mm。在本实施方式中,所述第一侵蚀高度优选为100mm,所述第二侵蚀高度优选为200mm。In the above process, the first erosion height and the second erosion height can be adjusted according to the actual situation of the converter. Generally speaking, in order to maintain the uniformity of the erosion of the converter lining and the safety of the use of the furnace lining, the first erosion height and the second erosion height can be adjusted according to the actual situation of the converter. For converters with long furnace age, the first erosion height and the second erosion height can be reduced. If the converter age is greater than 8000 times, the first erosion height can be 80mm, and the second erosion height can be 180mm; if the converter age is less than 4000 times, the second erosion height The first erosion height may be 120mm, and the second erosion height may be 220mm. In this embodiment, the first erosion height is preferably 100 mm, and the second erosion height is preferably 200 mm.
优选地,所述溅渣补炉方法还包括:当转炉炉底炉衬被侵蚀高度超过第一侵蚀高度但未超过第二侵蚀高度时,在采用调渣溅渣工艺对转炉实施溅渣操作后,判断底吹风口处是否有凹陷,若有凹陷,则采用补炉料快补炉工艺对转炉实施补炉操作,若无凹陷,则采用渣补炉工艺对转炉实施补炉操作。在转炉正常高节奏连续生产过程中,转炉不停歇的情况下,并没有过多的时间做补炉操作,因此只采用调渣溅渣工艺对转炉实施溅渣操作;然而当生产节奏较慢时,转炉有停歇的时间,在这样的情况下可在溅渣操作后对转炉进行补炉操作,从而使转炉得到充分的维护。Preferably, the slag splashing repairing method further comprises: when the eroded height of the bottom lining of the converter exceeds the first erosion height but does not exceed the second erosion height, after the slag splashing operation is performed on the converter using the slag-adjusting and slag-splashing process, It is judged whether there is a depression at the bottom air outlet. If there is a depression, the converter is repaired by the fast charging process of the charging material. If there is no depression, the converter is repaired by the slag repairing process. In the normal high-rhythm continuous production process of the converter, under the condition that the converter does not stop, there is not too much time for the repairing operation, so only the slag-adjusting and slag-splashing process is used to carry out the slag splashing operation on the converter; however, when the production rhythm is slow , the converter has a stop time, in this case, the converter can be repaired after the slag splashing operation, so that the converter can be fully maintained.
所述先倒渣后溅渣工艺包括:倒出炉渣渣量的1/3~1/2;降低氧枪高度至冷却枪位,氧枪对炉渣实施吹氮气冷却操作;随后,降低氧枪高度至溅渣枪位,氧枪对炉渣实施吹氮气溅渣操作。先倒渣后溅渣工艺的优点是能够缩短溅渣时间,炉渣在转炉内的留存时间不长,转炉底吹风口和炉底炉衬受侵蚀的时间则较短,从而能够对转炉底吹风口和炉底炉衬进行很好的维护,又降低溅渣成本。The process of pouring the slag first and then splashing the slag includes: pouring out 1/3-1/2 of the amount of slag; lowering the height of the oxygen lance to the cooling lance position, and the oxygen lance performs a nitrogen blowing cooling operation on the slag; then, lowering the height of the oxygen lance To the slag splashing gun position, the oxygen lance performs nitrogen blowing and slag splashing operation on the slag. The advantage of the process of pouring slag first and then splashing slag is that the time of slag splashing can be shortened. The furnace bottom lining is well maintained and the cost of slag splashing is reduced.
所述调渣溅渣工艺包括:判断转炉出钢后炉渣量是否充足,判断炉渣是否充足的依据是炉渣量是否大于转炉容量的1/10,若是,则先倒出炉渣渣量的1/3~1/2;随后,降低氧枪高度至溅渣枪位,氧枪对炉渣实施吹氮气溅渣操作,吹氮气溅渣操作开始后,通常在1min时间内,加入石灰石500~1000kg;随后,在吹氮气溅渣操作过程中加入白云石500~1000kg,并控制氧枪实施滑枪操作。调渣溅渣工艺的优点是通过调整炉渣,提高炉渣中MgO的含量,降低转炉底吹风口和炉底炉衬的侵蚀速度,同时还缩短溅渣时间,提高转炉运行效率。The slag adjusting and splashing process includes: judging whether the amount of slag is sufficient after the converter is tapped, and the basis for judging whether the amount of slag is sufficient is whether the amount of slag is greater than 1/10 of the capacity of the converter, and if so, first pour out 1/3 of the amount of slag ~1/2; then, lower the height of the oxygen lance to the slag splashing lance position, and the oxygen lance performs nitrogen blowing and slag splashing operation on the slag. After the nitrogen blowing slag splashing operation starts, usually within 1min, add limestone 500~1000kg; then, 500-1000kg of dolomite was added during the nitrogen blowing and slag splashing operation, and the oxygen lance was controlled to carry out the sliding lance operation. The advantage of the slag adjustment and splashing process is that by adjusting the slag, the content of MgO in the slag is increased, the erosion rate of the air outlet at the bottom of the converter and the lining of the furnace bottom is reduced, and the slag splashing time is shortened and the operation efficiency of the converter is improved.
所述渣补炉工艺包括:溅渣操作结束后实施摇炉挂渣操作;摇炉挂渣操作结束并且经过一段静置时间后实施炉渣冷却补炉操作。渣补炉工艺的优点是利用溅渣后的炉渣MgO含量高的特点,通过一段静置时间后可在底吹风口和炉底炉衬上 覆盖一层炉渣,减缓转炉底吹风口和炉底耐材的侵蚀速度,同时保持底吹风口的透气性。The slag repairing process includes: after the slag splashing operation is completed, the shaking furnace slag hanging operation is performed; after the shaking furnace slag hanging operation is completed and a period of standing time is passed, the slag cooling and furnace repairing operation is performed. The advantage of the slag repair process is that the slag after slag splashing has a high content of MgO. After a period of standing time, a layer of slag can be covered on the bottom air vent and the furnace bottom lining to slow down the converter bottom air vent and furnace bottom refractories. erosion rate while maintaining the breathability of the bottom air vents.
所述补炉料快补炉工艺包括:倒掉全部炉渣;向炉内加入补炉料,待补炉料熔化后摇炉使补炉料流淌至所需补炉的位置处。补炉料快补炉工艺的优点是,补炉料的流动性好且烧结速度快,因此用补炉料补炉的速度快、对炉底凹陷处的修补质量高、抗侵蚀性能好,可减缓转炉底吹风口和炉底炉衬的熔损速度。The rapid furnace repairing process of the charging material includes: pouring out all the slag; adding the charging charging material into the furnace, and shaking the furnace after the charging charging material is melted, so that the charging charging material flows to the position where the charging furnace is required. The advantages of the quick repairing process with the repairing charge are that the fluidity of the repairing charge is good and the sintering speed is fast, so the speed of repairing the furnace with the repairing charge is fast, the repair quality of the depression in the bottom of the furnace is high, and the corrosion resistance is good, which can slow down the bottom of the converter. Melting loss rate of blow vent and furnace bottom lining.
在本实施方式中,虽然只是对炉底炉衬被侵蚀高度进行判断,但炉底炉衬被侵蚀高度事实上也能反映底吹风口的侵蚀程度。也就是说,本实施方式的溅渣补炉方法所针对的维护对象包括炉底和底吹风口。In the present embodiment, although only the eroded height of the furnace bottom lining is judged, the eroded height of the furnace bottom lining can actually reflect the degree of erosion of the bottom blowing port. That is to say, the maintenance objects targeted by the slag splashing and furnace repairing method in this embodiment include the furnace bottom and the bottom air outlet.
本实施方式的溅渣补炉方法通过改进溅渣和补炉工艺,使溅渣时间缩短,并根据转炉底吹风口和炉底炉衬侵蚀速度,采用与转炉生产节奏相匹配的转炉溅渣和补炉工艺,既控制了转炉炉底炉衬和底吹风口的被侵蚀速度,又保证了底吹风口的冶金效果,从而提升了转炉底吹效率,延长了底吹风口的寿命,实现了底吹风口寿命与转炉炉龄同步的目的。The slag splashing and furnace repairing method of the present embodiment shortens the slag splashing time by improving the slag splashing and furnace repairing processes, and adopts the converter slag splashing and repairing methods that match the production rhythm of the converter according to the blowing port at the bottom of the converter and the erosion rate of the furnace bottom lining. The furnace process not only controls the erosion rate of the bottom lining of the converter and the bottom blowing port, but also ensures the metallurgical effect of the bottom blowing port, thereby improving the bottom blowing efficiency of the converter, prolonging the life of the bottom blowing port, and realizing the bottom blowing port. The purpose of synchronizing the service life with the age of the converter.
以下针对不同炉底侵蚀情况给出具体实施例。Specific examples are given below for different furnace bottom erosion conditions.
实施例1:Example 1:
以公称容量300t(吨)、底吹8支路转炉为例,对该转炉实施本发明的溅渣补炉方法。Taking a converter with a nominal capacity of 300 t (tons) and bottom blowing 8 branches as an example, the converter is implemented with the slag splashing repair method of the present invention.
第一侵蚀高度设定为100mm,当转炉炉底炉衬被侵蚀高度<100mm时,即转炉炉底炉衬被侵蚀高度未超过第一侵蚀高度,则实施先倒渣后溅渣工艺,实施过程为:The first erosion height is set to 100mm. When the eroded height of the converter bottom lining is less than 100mm, that is, the eroded height of the converter bottom lining does not exceed the first erosion height, the process of pouring slag first and then splashing slag is implemented. The implementation process is as follows:
转炉出钢结束,摇炉并观察炉渣量,然后继续摇炉倒出炉渣量1/3。After the converter tapping is completed, shake the furnace and observe the amount of slag, and then continue to shake the furnace to pour out 1/3 of the amount of slag.
摇炉至零位,降低氧枪高度至冷却枪位,氧枪开氮气对炉渣实施吹氮气冷却操作,冷却操作维持10~30秒。Shake the furnace to the zero position, lower the height of the oxygen lance to the cooling lance position, and open the oxygen lance to blow nitrogen to cool the slag. The cooling operation is maintained for 10 to 30 seconds.
降低氧枪高度至溅渣枪位,氧枪对炉渣实施吹氮气溅渣操作,溅渣操作维持60~120秒。Lower the height of the oxygen lance to the position of the slag splashing lance, and the oxygen lance performs the nitrogen blowing and slag splashing operation on the slag, and the slag splashing operation is maintained for 60-120 seconds.
在上述溅渣过程中,转炉实施底吹供气,供气流量随时间逐步调大,具体为:0~60秒阶段为1200Nm 3/h;60~120秒阶段为1400Nm 3/h;120秒至结束阶段为1600Nm 3/h。 During the above-mentioned slag splashing process, the converter implements bottom blowing air supply, and the air supply flow is gradually increased with time, specifically: 1200Nm 3 /h in the stage of 0-60 seconds; 1400Nm 3 /h in the stage of 60-120 seconds; 120 seconds 1600Nm 3 /h to the end stage.
实施例2:Example 2:
以公称容量300t、底吹8支路转炉为例,对该转炉实施本发明的溅渣补炉方法。Taking a converter with a nominal capacity of 300t and 8 branches of bottom blowing as an example, the converter is implemented with the slag splashing repair method of the present invention.
第一侵蚀高度设定为100mm,第二侵蚀高度设定为200mm,当转炉炉底炉衬被侵蚀高度大于100mm但小于200mm时,即转炉炉底炉衬被侵蚀高度超过第一侵蚀高度但未超过第二侵蚀高度时,且转炉的生产节奏紧张,则实施调渣溅渣工艺,实施过程为:The first erosion height is set to 100mm, and the second erosion height is set to 200mm. When the eroded height of the converter bottom lining is greater than 100mm but less than 200mm, that is, the eroded height of the converter bottom lining exceeds the first erosion height but does not exceed the first erosion height. Second, when the erosion height is high and the production rhythm of the converter is tense, the slag adjustment and slag splashing process is implemented. The implementation process is as follows:
转炉出钢结束,摇炉并观察炉渣量是否充足,即判断炉渣量是否大于转炉容量的1/10,判断渣量充足则继续摇炉倒出炉渣量1/2。After the converter is tapped, shake the furnace and observe whether the amount of slag is sufficient, that is, to determine whether the amount of slag is greater than 1/10 of the capacity of the converter, and if the amount of slag is sufficient, continue to shake the furnace to pour out 1/2 of the amount of slag.
摇炉至零位,降低氧枪高度至溅渣枪位,氧枪对炉渣实施吹氮气溅渣操作,吹氮气溅渣操作开始后,加入石灰石500kg。Shake the furnace to the zero position, lower the height of the oxygen lance to the slag splashing lance position, and the oxygen lance performs nitrogen blowing and slag splashing operation on the slag. After the nitrogen blowing and slag splashing operation starts, 500kg of limestone is added.
当吹氮气溅渣操作进行到30~90秒阶段内加入白云石1000kg。When the nitrogen blowing and splashing operation is carried out to the stage of 30 to 90 seconds, 1000 kg of dolomite is added.
控制氧枪枪位进行滑枪操作。Control the oxygen lance position for slide gun operation.
在上述溅渣过程中,转炉实施底吹供气,供气流量随时间逐步调整,具体为:0~30秒阶段为1000Nm 3/h;30~120秒阶段为800Nm 3/h;120秒至结束阶段为1200Nm 3/h。其中,在30~120秒阶段减少了底吹供气流量,这是为了利用炉渣的热量将此阶段加入的白云石充分熔化,如果供气流量高则不利于白云石的熔化。 In the process of slag splashing, gas bottom blowing converter embodiments, gas flow rate gradually adjusted over time, specifically: 0 to 30 seconds stage 1000Nm 3 / h; 30 ~ 120 seconds stage 800Nm 3 / h; 120 seconds The end stage is 1200Nm 3 /h. Among them, the bottom blowing air supply flow rate was reduced in the 30-120 second stage, in order to fully melt the dolomite added in this stage by using the heat of the slag. If the air supply flow rate is high, it is not conducive to the melting of the dolomite.
实施例3Example 3
以公称容量300t、底吹8支路转炉为例,对该转炉实施本发明的溅渣补炉方法。Taking a converter with a nominal capacity of 300t and 8 branches of bottom blowing as an example, the converter is implemented with the slag splashing repair method of the present invention.
第一侵蚀高度设定为100mm,第二侵蚀高度设定为200mm,当转炉炉底炉衬被侵蚀高度大于100mm但小于200mm时,即转炉炉底炉衬被侵蚀高度超过第一侵蚀高度但未超过第二侵蚀高度时,且转炉的生产节奏不紧张,转炉有停歇时间,则实施调渣溅渣工艺后再渣补炉工艺,实施过程为:The first erosion height is set to 100mm, and the second erosion height is set to 200mm. When the eroded height of the converter bottom lining is greater than 100mm but less than 200mm, that is, the eroded height of the converter bottom lining exceeds the first erosion height but does not exceed the first erosion height. Second, when the erosion height is high, and the production rhythm of the converter is not tense, and the converter has a stop time, the slag adjustment and slag splashing process is carried out and then the slag repair process is carried out. The implementation process is as follows:
转炉出钢结束,判断炉渣量并不充足,则不倒炉渣。When the converter is finished tapping, if it is judged that the amount of slag is not sufficient, the slag will not be poured.
摇炉至零位,降低氧枪高度至溅渣枪位,氧枪对炉渣实施吹氮气溅渣操作,吹氮气溅渣操作开始后,加入石灰石1000kg。Shake the furnace to the zero position, lower the height of the oxygen lance to the slag splashing lance position, and the oxygen lance performs nitrogen blowing and slag splashing operation on the slag. After the nitrogen blowing slag splashing operation starts, 1000kg of limestone is added.
当吹氮气溅渣操作进行到60~120秒阶段内加入白云石1000kg。When the nitrogen blowing slag splashing operation is carried out to the stage of 60 to 120 seconds, 1000 kg of dolomite is added.
控制氧枪进行滑枪操作。Control the oxygen lance for slide gun operation.
在上述吹氮气溅渣操作过程中,转炉实施底吹供气,供气流量随时间逐步调整,具体流量同实施例2一致。During the above-mentioned nitrogen blowing and slag splashing operation, the converter implements bottom blowing and gas supply, and the gas supply flow rate is gradually adjusted over time, and the specific flow rate is the same as that in Example 2.
溅渣操作结束后实施摇炉挂渣操作,前后摇炉来回挂渣1~3次。After the slag splashing operation is completed, the slag hanging operation of the shaking furnace is carried out, and the slag hanging back and forth of the shaking furnace is 1 to 3 times.
摇炉挂渣操作结束后摇炉至零位,经过一段20~40分钟的静置时间后实施炉渣冷却补炉操作。After the slag hanging operation of the shaking furnace is completed, the furnace is shaken to the zero position, and the slag cooling and furnace repairing operation is carried out after a period of 20-40 minutes of standing time.
在所述静置时间及后续炉渣冷却补炉过程中,转炉继续实施底吹供气,供气流量随时间逐步调大,具体流量为:0~5分钟阶段为560Nm 3/h;5~10分钟阶段为640Nm 3/h;10~20分钟阶段为800Nm 3/h;20分钟至结束阶段为1000Nm 3/h。 During the standing time and the subsequent slag cooling and repairing process, the converter continues to implement bottom blowing gas supply, and the gas supply flow rate is gradually increased with time. The specific flow rate is: 560Nm 3 /h in the stage of 0-5 minutes; The minute stage is 640Nm 3 /h; the 10-20 minute stage is 800Nm 3 /h; the 20-minute to end stage is 1000Nm 3 /h.
实施例4Example 4
以公称容量300t、底吹8支路转炉为例,对该转炉实施本发明的溅渣补炉方法。Taking a converter with a nominal capacity of 300t and 8 branches of bottom blowing as an example, the converter is implemented with the slag splashing repair method of the present invention.
第二侵蚀高度设定为200mm,当转炉炉底炉衬被侵蚀高度大于200mm时,即转炉炉底炉衬被侵蚀高度超过第二侵蚀高度,则实施补炉料快补炉工艺,实施过程为:The second erosion height is set to 200mm. When the eroded height of the converter bottom lining is greater than 200mm, that is, the eroded height of the converter bottom lining exceeds the second erosion height, the fast-repairing process of the charging material is implemented. The implementation process is as follows:
转炉出钢结束,摇炉倒掉全部炉渣。After the tapping of the converter is completed, all the slag is poured out by shaking the furnace.
摇炉至炉口朝向侧面,向炉内加入快速补炉料2包(每包700kg)。Shake the furnace until the mouth of the furnace faces the side, and add 2 bags (700kg per bag) of fast charging materials into the furnace.
待补炉料熔化,摇炉使补炉料流淌至所需补炉的凹坑处,或前后摇炉使补炉料涂于炉底。When the charging material is melted, shake the furnace to make the charging material flow to the pit of the required charging furnace, or shake the furnace back and forth so that the charging charging material is coated on the bottom of the furnace.
在上述补炉过程中,转炉实施底吹供气,供气流量随时间逐步调大,具体为:0~5分钟阶段为480Nm 3/h;5~10分钟阶段为720Nm 3/h;10~20分钟阶段为800Nm 3/h;20分钟至结束阶段为1000Nm 3/h。 In the fettling process gas bottom blowing converter embodiments, gas flow rate over time to gradually turn up, specifically: Phase 0 to 5 minutes was 480Nm 3 / h; 5 ~ 10 minutes in a stepwise was 720Nm 3 / h; 10 ~ 20 minutes stage 800Nm 3 / h; 20 minutes to end phase of 1000Nm 3 / h.
以上仅为本发明的较佳实施例而已,并非用于限定本发明的保护范围,因此,凡在本发明的精神和原则之内所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above are only preferred embodiments of the present invention, and are not intended to limit the protection scope of the present invention. Therefore, any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the present invention. within the scope of protection of the invention.
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| JP2019019381A (en) * | 2017-07-18 | 2019-02-07 | 株式会社神戸製鋼所 | Repairing method of refractories applied to bottom-blown tuyere of converter-type reaction vessel |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112921144A (en) * | 2021-01-25 | 2021-06-08 | 山东莱钢永锋钢铁有限公司 | Method for melting slag by using furnace slag |
| CN115261548A (en) * | 2022-06-08 | 2022-11-01 | 日照钢铁控股集团有限公司 | Method for improving slag splashing furnace protection effect of converter high-oxidability furnace slag |
| CN115261548B (en) * | 2022-06-08 | 2024-03-01 | 日照钢铁控股集团有限公司 | Method for improving splashing slag protection effect of high-oxidability slag of converter |
| CN115323104A (en) * | 2022-07-23 | 2022-11-11 | 阳春新钢铁有限责任公司 | Automatic slag splashing furnace protection method for converter |
| CN115323104B (en) * | 2022-07-23 | 2024-03-19 | 阳春新钢铁有限责任公司 | Automatic slag splashing furnace protection method for converter |
| CN115404302A (en) * | 2022-08-30 | 2022-11-29 | 湖南湘钢瑞泰科技有限公司 | Converter fettling method |
| CN115404302B (en) * | 2022-08-30 | 2023-11-10 | 湖南湘钢瑞泰科技有限公司 | Converter repairing method |
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| CN113930574B (en) | 2022-12-16 |
| CN113930574A (en) | 2022-01-14 |
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