TWI439551B - Inhibition method of converter - Google Patents

Inhibition method of converter Download PDF

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TWI439551B
TWI439551B TW100104600A TW100104600A TWI439551B TW I439551 B TWI439551 B TW I439551B TW 100104600 A TW100104600 A TW 100104600A TW 100104600 A TW100104600 A TW 100104600A TW I439551 B TWI439551 B TW I439551B
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slag
molten iron
steelmaking
converter
overflow
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TW100104600A
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TW201233811A (en
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China Steel Corp
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Description

轉爐煉鋼浮溢的抑制方法Method for suppressing overflow of steelmaking in converter

本發明是有關於一種轉爐煉鋼方法,特別是指一種轉爐煉鋼浮溢的抑制方法。The invention relates to a converter steelmaking method, in particular to a method for suppressing the overflow of steelmaking in a converter.

現有轉爐煉鋼方法是將高爐產製出的高矽鐵水送入轉爐中,並藉由吹氧、造渣的方式將該鐵水中的雜質析出,然而在吹氧時,氧氣灌入鐵水中會造成鐵水翻騰而溢出轉爐外。The existing converter steelmaking method is to feed the sorghum molten iron produced by the blast furnace into the converter, and to precipitate the impurities in the molten iron by blowing oxygen and slagging, but when oxygen is blown, the oxygen is poured into the molten iron. It will cause the molten iron to churn and overflow outside the converter.

有業者為了改善上述缺點,而提出如圖1所示的另一種現有轉爐煉鋼方法1,包含一預處理步驟11,以及一煉鋼步驟12。在該預處理步驟11中是先將由高爐產製出的鐵水進行降矽處理,接著再將降矽後體積已減少的鐵水送入轉爐內進行煉鋼步驟12。然而,預處理步驟11會造成由高爐產出的高溫鐵水溫度降低,因此該鐵水在送入轉爐之後要重新升溫而會造成能量的損耗。In order to improve the above disadvantages, another prior art converter steelmaking method 1 as shown in FIG. 1 is proposed, which includes a pretreatment step 11 and a steelmaking step 12. In the pretreatment step 11, the molten iron produced by the blast furnace is first subjected to a helium reduction treatment, and then the molten iron having a reduced volume after the helium reduction is sent to the converter for the steelmaking step 12. However, the pretreatment step 11 causes a decrease in the temperature of the high temperature molten iron produced by the blast furnace, so that the molten iron is heated again after being sent to the converter to cause energy loss.

所以,如何改善以上所述的缺點,一直是本技術領域者持續努力的重要目標。Therefore, how to improve the above-mentioned shortcomings has been an important goal of continuous efforts by those skilled in the art.

因此,本發明之目的,即在提供一種能避免爐渣溢出轉爐外的轉爐煉鋼浮溢的抑制方法。Accordingly, it is an object of the present invention to provide a method of suppressing the overflow of steelmaking in a converter outside the converter.

於是,本發明轉爐煉鋼浮溢的抑制方法包含一初成渣步驟、一預排渣步驟,以及一次成渣步驟。Therefore, the method for suppressing the overflow of the converter steelmaking according to the present invention comprises a preliminary slag step, a pre-slag slag step, and a slagging step.

該初成渣步驟是將一氣體與一造渣劑送入一裝盛有一鐵水的轉爐內,使該鐵水中的雜質與該氣體、造渣劑反應而形成一浮於該鐵水表面的爐渣,並調整使該爐渣的鹽基度為1.0至1.4,該鐵水的溫度為1350℃至1450℃。The preliminary slag step is to feed a gas and a slagging agent into a converter containing a molten iron, and react the impurities in the molten iron with the gas and the slag forming agent to form a floating surface of the molten iron. The slag is adjusted so that the slag has a base degree of 1.0 to 1.4, and the temperature of the molten iron is 1350 ° C to 1450 ° C.

該預排渣步驟是將該初成渣步驟所形成的部分爐渣排出該轉爐外。The pre-slag discharging step is to discharge a part of the slag formed by the preliminary slag forming step outside the converter.

該次成渣步驟是以高於該初成渣步驟的流量將該氣體送入該預排渣步驟之後的鐵水中。The slagging step is to feed the gas into the molten iron after the pre-slag discharging step at a flow rate higher than the preliminary slag forming step.

本發明的功效在於:本發明轉爐煉鋼浮溢的抑制方法是藉由低鹽基度的造渣方式配合適當的溫度以使爐渣維持良好流動性,以避免產生浮溢現象,該預排渣步驟進一步將該初成渣步驟所形成的部分爐渣排出該轉爐外,藉此減少該轉爐內的爐渣體積,因此在該次成渣步驟中就能將高流量的氣體送入該鐵水中而能避免浮於該鐵水表面的爐渣溢出該轉爐外。The effect of the invention is that the method for suppressing the overflow of the converter steelmaking according to the invention is to maintain a good fluidity of the slag by using a low-salt base slagging method to match the appropriate temperature to avoid the occurrence of a floating phenomenon, the pre-slag Step further discharging a part of the slag formed by the initial slag forming step outside the converter, thereby reducing the volume of the slag in the converter, so that a high-flow gas can be sent into the molten iron in the slagging step. The slag floating on the surface of the molten iron is prevented from overflowing outside the converter.

有關本發明之前述及其他技術內容、特點與功效,在以下配合參考圖式之一個較佳實施例的詳細說明中,將可清楚的呈現。The above and other technical contents, features and advantages of the present invention will be apparent from the following detailed description of the preferred embodiments.

參閱圖2與圖3,為本發明轉爐煉鋼浮溢的抑制方法的較佳實施例,包含一初成渣步驟2、一預排渣步驟3,以及一次成渣步驟4。Referring to FIG. 2 and FIG. 3, a preferred embodiment of the method for suppressing the overflow of steelmaking in a converter according to the present invention comprises a preliminary slag step 2, a pre-slag slag step 3, and a slagging step 4.

該初成渣步驟2是將一氣體24與一造渣劑25送入一裝盛有一鐵水22的轉爐21內,使該鐵水22中的雜質與該氣體24、造渣劑25反應而形成一浮於該鐵水22表面的爐渣23。在本較佳實施例中,該氣體24為氧氣(O2 );該造渣劑25為石灰(氧化鈣CaO);而該鐵水22則是由高爐產製出的高矽鐵水22,特別說明的是,本較佳實施例所謂的高矽鐵水22是指矽含量大於1.0%的鐵水22。The preliminary slag step 2 is to feed a gas 24 and a slagging agent 25 into a converter 21 containing a molten iron 22, and react the impurities in the molten iron 22 with the gas 24 and the slag forming agent 25. A slag 23 floating on the surface of the molten iron 22 is formed. In the preferred embodiment, the gas 24 is oxygen (O 2 ); the slagging agent 25 is lime (calcium oxide CaO); and the molten iron 22 is sorghum hot metal 22 produced by the blast furnace. Specifically, the so-called sorghum hot metal 22 of the preferred embodiment refers to molten iron 22 having a cerium content of more than 1.0%.

特別說明的是,一般而言該鐵水22所含的主要雜質通常為碳(C)、矽(Si)、錳(Mn)、磷(P)、硫(S)等,通入氧氣主要是為了使雜質氧化,而該石灰則能與氧化矽(SiO2 )反應並形成爐渣23。因此,在本較佳實施例中,該初成渣步驟2主要的目的是用以脫矽,因此這個階段也可以稱為脫矽期,會形成含矽量較高的爐渣23。另外,在本較佳實施例中,是以頂吹法送入氧氣,並以底吹法送入惰性氣體,底吹法所送入的惰性氣體能協助攪拌該鐵水22以利氧氣均勻地與該鐵水22內的雜質反應。In particular, in general, the main impurities contained in the molten iron 22 are usually carbon (C), cerium (Si), manganese (Mn), phosphorus (P), sulfur (S), etc., and the introduction of oxygen is mainly In order to oxidize the impurities, the lime can react with cerium oxide (SiO 2 ) and form slag 23 . Therefore, in the preferred embodiment, the primary purpose of the preliminary slag step 2 is to dislocate, so this stage may also be referred to as the dislocation period, and a slag 23 having a higher amount of strontium may be formed. In addition, in the preferred embodiment, the oxygen is fed by the top blowing method, and the inert gas is fed by the bottom blowing method, and the inert gas fed by the bottom blowing method can assist the stirring of the molten iron 22 to facilitate the uniformity of oxygen. It reacts with impurities in the molten iron 22.

該預排渣步驟3是將該初成渣步驟2所形成的部分爐渣23排出該轉爐21外。在本較佳實施例中,以整體爐渣23的重量百分比為100wt%計,是將30wt%至50wt%的爐渣23排出該轉爐21外。實際作業時,是由該轉爐21頂部開口將浮於該鐵水22表面的爐渣23倒出,因此不易將全部的爐渣23排出,而排出30wt%至50wt%的爐渣23能顯著地減少後續的浮溢現象。The pre-slag discharging step 3 is to discharge a part of the slag 23 formed in the preliminary slag step 2 to the outside of the converter 21. In the preferred embodiment, 30% by weight to 50% by weight of the slag 23 is discharged from the outside of the converter 21, based on 100% by weight of the total slag 23. In actual operation, the slag 23 floating on the surface of the molten iron 22 is poured out from the top opening of the converter 21, so that it is difficult to discharge all the slag 23, and discharging 30% to 50% by weight of the slag 23 can significantly reduce the subsequent slag. Floating phenomenon.

該次成渣步驟4是以高於該初成渣步驟2的流量將該氣體24送入該預排渣步驟3之後的鐵水22中。特別說明的是,在本較佳實施例中,該次成渣步驟4主要的目的是用以脫碳以及其他雜質,因此這個階段也可以稱為脫碳期,會形成含碳量較高的爐渣23。This slagging step 4 feeds the gas 24 into the molten iron 22 after the pre-slag slag step 3 at a flow rate higher than the slag forming step 2. In particular, in the preferred embodiment, the primary purpose of the slagging step 4 is to decarburize and other impurities, so this stage may also be referred to as a decarburization period, which results in a higher carbon content. Slag 23

參閱表1,為本發明轉爐煉鋼浮溢的抑制方法的實驗例與比較例。Referring to Table 1, an experimental example and a comparative example of a method for suppressing the overflow of steelmaking in a converter according to the present invention are shown.

由表1可知,該初成渣步驟2中,該爐渣23的鹽基度在1.0至1.4之間較佳,因為當鹽基度大於1.4時,浮溢的情況會較為明顯,而鹽基度小於1.0時,會有成渣量過少的情況而影響煉鋼效率。在本較佳實施例中,該鐵水22的溫度為1350℃至1450℃,因為當溫度高於1450℃時,較容易產生浮溢現象。綜上所述,同時符合鹽基度介於1.0至1.4與鐵水22溫度介於1350℃至1450℃兩個條件時,能夠最有效地抑制浮溢現象,超出上述鹽基度與溫度範圍時,浮溢現象會較為明顯。It can be seen from Table 1 that in the preliminary slag step 2, the salt base degree of the slag 23 is preferably between 1.0 and 1.4, because when the base degree of the salt is more than 1.4, the floating condition is more obvious, and the salt base degree is more obvious. When it is less than 1.0, the slag amount may be too small to affect the steelmaking efficiency. In the preferred embodiment, the temperature of the molten iron 22 is from 1350 ° C to 1450 ° C, because when the temperature is higher than 1450 ° C, the floating phenomenon is more likely to occur. In summary, when the salt base degree is between 1.0 and 1.4 and the temperature of the molten iron 22 is between 1350 ° C and 1450 ° C, the floating phenomenon can be most effectively suppressed. When the above-mentioned salt base degree and temperature range are exceeded, The phenomenon of floating will be more obvious.

較佳地,在該初成渣步驟2中,氧氣流量為25000~35000Nm3 /hr,惰性氣體流量為500~1000Nm3 /hr。在該次成渣步驟4中,氧氣流量為45000~60000Nm3 /hr,惰性氣體流量為300~2000Nm3 /hr。當然,該次成渣步驟4的頂吹氧氣流量大於該初成渣步驟2的頂吹氧氣流量,而該次成渣步驟4的底吹惰性氣體流量則小於該初成渣步驟2的底吹惰性氣體流量也可以達成相同的目的。Preferably, in the preliminary slag step 2, the oxygen flow rate is 25000 to 35000 Nm 3 /hr, and the inert gas flow rate is 500 to 1000 Nm 3 /hr. In the slagging step 4, the oxygen flow rate is 45,000 to 60000 Nm 3 /hr, and the inert gas flow rate is 300 to 2000 Nm 3 /hr. Of course, the top blowing oxygen flow rate of the slagging step 4 is greater than the top blowing oxygen flow rate of the preliminary slag step 2, and the bottom blowing inert gas flow rate of the secondary slag forming step 4 is smaller than the bottom blowing of the preliminary slag step 2 The inert gas flow can also achieve the same purpose.

特別說明的是,當然在該次成渣步驟4之後,還會再將該爐渣23與鐵水22分離,然而在該次成渣步驟4之後的後續作業方式與現有技術相同,此為本技術領域中具有通常知識者所熟知,因此不予贅述。It is to be noted that, of course, after the slagging step 4, the slag 23 is separated from the molten iron 22, however, the subsequent operation after the slag forming step 4 is the same as the prior art, which is the present technology. It is well known to those of ordinary skill in the art and therefore will not be described.

另外,本發明轉爐煉鋼浮溢的抑制方法除了能用於一般轉爐煉鋼製程,以得到具有良好流動性的爐渣23,進而能避免產生浮溢現象。當然,本發明轉爐煉鋼浮溢的抑制方法也能應用於大修或新建的高爐初產的鐵水22,因為大修或新建後的高爐所產出的鐵水22含矽量通常偏高,因此通常會以倒地方式處理,以本發明抑制方法進行處理可以減少倒地廢鋼量。In addition, the method for suppressing the overflow of the converter steelmaking according to the present invention can be used in the general converter steelmaking process to obtain the slag 23 having good fluidity, thereby avoiding the occurrence of a floating phenomenon. Of course, the method for suppressing the overflow of steelmaking in the converter of the present invention can also be applied to the molten iron 22 produced in the overhauled or newly built blast furnace, because the amount of strontium 22 produced by the blast furnace after overhaul or new construction is usually high, so It is usually treated in an inverted manner, and the treatment by the suppression method of the present invention can reduce the amount of scrapped steel.

綜上所述,本發明轉爐煉鋼浮溢的抑制方法是藉由低鹽基度的造渣方式配合適當的溫度以使爐渣23維持良好流動性,以避免產生浮溢現象,該預排渣步驟3進一步將該初成渣步驟2所形成的部分爐渣23排出該轉爐21外,藉此減少該轉爐21內的爐渣23體積,因此在該次成渣步驟4中就能將高流量的氣體24送入該鐵水22中而能避免浮於該鐵水22表面的爐渣23溢出該轉爐21外,故確實能達成本發明之目的。In summary, the method for suppressing the overflow of steelmaking in the converter of the present invention is to maintain a good fluidity of the slag 23 by a slag forming method with a low salt base to maintain a good fluidity to avoid the occurrence of a floating slag. Step 3 further discharges part of the slag 23 formed in the preliminary slag step 2 out of the converter 21, thereby reducing the volume of the slag 23 in the converter 21, so that a high-flow gas can be obtained in the slag forming step 4. The feed of the molten iron 22 into the molten iron 22 prevents the slag 23 floating on the surface of the molten iron 22 from overflowing the outside of the converter 21, so that the object of the present invention can be achieved.

惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,即大凡依本發明申請專利範圍及發明說明內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。The above is only the preferred embodiment of the present invention, and the scope of the invention is not limited thereto, that is, the simple equivalent changes and modifications made by the scope of the invention and the description of the invention are All remain within the scope of the invention patent.

2...初成渣步驟2. . . Initial slag step

21...轉爐twenty one. . . Converter

22...鐵水twenty two. . . molten iron

23...爐渣twenty three. . . Slag

24...氣體twenty four. . . gas

25...造渣劑25. . . Slag forming agent

3...預排渣步驟3. . . Pre-slag removal step

4...次成渣步驟4. . . Secondary slag step

圖1是一流程圖,說明現有轉爐煉鋼方法;Figure 1 is a flow chart illustrating a conventional converter steelmaking method;

圖2是一流程圖,說明本發明轉爐煉鋼浮溢的抑制方法的較佳實施例;以及Figure 2 is a flow chart showing a preferred embodiment of the method for suppressing the overflow of steelmaking in the present invention;

圖3是一示意圖,輔助說明該較佳實施例。Figure 3 is a schematic diagram of the preferred embodiment.

2...初成渣步驟2. . . Initial slag step

3...預排渣步驟3. . . Pre-slag removal step

4...次成渣步驟4. . . Secondary slag step

Claims (10)

一種轉爐煉鋼浮溢的抑制方法,包含:一初成渣步驟,將一氣體與一造渣劑送入一裝盛有一鐵水的轉爐內,使該鐵水中的雜質與該氣體、造渣劑反應而形成一浮於該鐵水表面的爐渣,並調整使該爐渣的鹽基度為1.0至1.4,該鐵水的溫度為1350℃至1450℃;一預排渣步驟,將該初成渣步驟所形成的部分爐渣排出該轉爐外;以及一次成渣步驟,以高於該初成渣步驟的流量將該氣體送入該預排渣步驟之後的鐵水中。A method for suppressing overflow of steelmaking in a converter comprises: a preliminary slagging step of feeding a gas and a slag forming agent into a converter containing a molten iron to make impurities in the molten iron and the gas and slagging The agent reacts to form a slag floating on the surface of the molten iron, and adjusts the slag to a base degree of 1.0 to 1.4, and the temperature of the molten iron is 1350 ° C to 1450 ° C; a pre-slag step, the preliminary Part of the slag formed by the slag step is discharged outside the converter; and a slagging step is performed to deliver the gas into the molten iron after the pre-slag step at a flow rate higher than the initial slag step. 根據申請專利範圍第1項所述轉爐煉鋼浮溢的抑制方法,其中,在該預排渣步驟中,以整體爐渣的重量百分比為100wt%計,是將30wt%至50wt%的爐渣排出該轉爐外。The method for suppressing the overflow of steelmaking in a converter according to the first aspect of the invention, wherein in the pre-slaging step, 30% by weight to 50% by weight of the slag is discharged as 100% by weight of the total slag Outside the converter. 根據申請專利範圍第1項所述轉爐煉鋼浮溢的抑制方法,其中,在該初成渣步驟中,是形成含矽量較高的爐渣,在該次成渣步驟中,是形成含碳量較高的爐渣。The method for suppressing the overflow of steelmaking in a converter according to the first aspect of the patent application, wherein in the preliminary slag step, slag having a high cerium content is formed, and in the slag forming step, carbon is formed A higher amount of slag. 根據申請專利範圍第1項所述轉爐煉鋼浮溢的抑制方法,其中,在該初成渣步驟中,該氣體包括一氧氣,該造渣劑為石灰。The method for suppressing the overflow of steelmaking in a converter according to the first aspect of the patent application, wherein in the preliminary slag step, the gas comprises an oxygen gas, and the slagging agent is lime. 根據申請專利範圍第4項所述轉爐煉鋼浮溢的抑制方法,其中,在該初成渣步驟中,是以頂吹法將該氧氣送入該鐵水內,並以底吹法將一惰性氣體送入該鐵水內。According to the method for suppressing the overflow of the steelmaking steel according to the fourth aspect of the patent application, in the preliminary slag step, the oxygen is sent into the molten iron by a top blowing method, and the bottom blowing method is used. An inert gas is fed into the molten iron. 根據申請專利範圍第5項所述轉爐煉鋼浮溢的抑制方法,其中,在該次成渣步驟中,是以頂吹法將該氧氣送入該鐵水內,並以底吹法將該惰性氣體送入該鐵水內。The method for suppressing the overflow of steelmaking in a converter according to the fifth aspect of the patent application, wherein in the step of forming the slag, the oxygen is fed into the molten iron by a top blowing method, and the bottom blowing method is used to An inert gas is fed into the molten iron. 根據申請專利範圍第4至6項中任一項所述轉爐煉鋼浮溢的抑制方法,其中,該次成渣步驟中頂吹法的氧氣流量大於該初成渣步驟中頂吹法的氧氣流量。The method for suppressing the overflow of steelmaking in a converter according to any one of claims 4 to 6, wherein the oxygen flow rate of the top blowing method in the slag forming step is greater than the oxygen of the top blowing method in the preliminary slag step flow. 根據申請專利範圍第4至6項中任一項所述轉爐煉鋼浮溢的抑制方法,其中,該次成渣步驟中底吹法的惰性氣體流量小於該初成渣步驟中底吹法的惰性氣體流量。The method for suppressing the overflow of steelmaking steel according to any one of claims 4 to 6, wherein the inert gas flow rate of the bottom blowing method in the slag forming step is smaller than the bottom blowing method in the preliminary slag step Inert gas flow. 根據申請專利範圍第4至6項中任一項所述轉爐煉鋼浮溢的抑制方法,其中,在該初成渣步驟中,氧氣流量為25000~35000Nm3 /hr,惰性氣體流量為500~1000Nm3 /hr。The method for suppressing the overflow of steelmaking in a converter according to any one of claims 4 to 6, wherein in the preliminary slag step, the oxygen flow rate is 25000 to 35000 Nm 3 /hr, and the inert gas flow rate is 500~ 1000Nm 3 /hr. 根據申請專利範圍第4至6項中任一項所述轉爐煉鋼浮溢的抑制方法,其中,在該次成渣步驟中,氧氣流量為45000~60000Nm3 /hr,惰性氣體流量為300~2000Nm3 /hr。The method for suppressing the overflow of steelmaking in a converter according to any one of claims 4 to 6, wherein in the step of forming the slag, the oxygen flow rate is 45,000 to 60000 Nm 3 /hr, and the inert gas flow rate is 300~ 2000 Nm 3 /hr.
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