Method for refining hot metal in converter
US-9957581-B2 · May 1, 2018 · US
US2024076754A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024076754-A1 |
| Application number | US-202118270617-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 21, 2021 |
| Priority date | Jan 26, 2021 |
| Publication date | Mar 7, 2024 |
| Grant date | — |
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A molten iron refining method having, an auxiliary material, and an oxidizing gas supplied through a top-blowing lance, to a cold iron source and molten pig iron that are contained/fed in a converter-type vessel, and molten iron is subjected to a refining process. A pre-charged cold iron source is charged into the converter-type vessel at an amount not larger than 0.15 times. A furnace-top-added cold iron source that's part or all of the cold iron source and added from a furnace top is fed during the refining process. A burner at a leading end of the top-blowing lance that spray holes through which a fuel and a combustion-supporting gas are ejected. During the refining process, a powdery auxiliary material processed into powder that's part of the auxiliary material is blown in, to pass through a flame formed by the burner.
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1 . A molten iron refining method in which an auxiliary material is added, and an oxidizing gas is supplied through a top-blowing lance, to a cold iron source and molten pig iron that are contained or fed in a converter-type vessel, and molten iron is subjected to a refining process, wherein: prior to the refining process, a pre-charged cold iron source that is part of the cold iron source and charged all at once into the converter-type vessel before the molten pig iron is charged into the converter-type vessel is charged in an amount not larger than 0.15 times a sum of an amount of the pre-charged cold iron source and a charge amount of the molten pig iron, or is not charged; a furnace-top-added cold iron source that is part or all of the cold iron source and added from a furnace top of the converter-type vessel is fed into the converter-type vessel during the refining process; a burner is further used that is provided at a leading end of the top-blowing lance or at a leading end of a second lance installed separately from the top-blowing lance, and that has spray holes through which a fuel and a combustion-supporting gas are ejected; and during at least part of a period of the refining process, a powdery auxiliary material or an auxiliary material processed into powder that is at least part of the auxiliary material is blown in so as to pass through a flame formed by the burner. 2 . The molten iron refining method according to claim 1 , wherein a longest dimension of the furnace-top-added cold iron source is not larger than 100 mm. 3 . The molten iron refining method according to claim 1 , wherein the refining process is a decarburization process of molten iron. 4 . The molten iron refining method according to claim 3 , wherein the refining process is a decarburization process that is performed with a converter-type vessel in which molten pig iron dephosphorized beforehand is charged. 5 . The molten iron refining method according to claim 1 , wherein the refining process is a dephosphorization process of molten iron. 6 . The molten iron refining method according to claim 5 , wherein one or both of the following conditions are met: that the concentration of carbon contained in the furnace-top-added cold iron source is not lower than 0.3 mass %, and that the temperature of the molten iron upon completion of the dephosphorization process is not lower than 1380° C. 7 . The molten iron refining method according to claim 1 , wherein: the refining process is a dephosphorization-decarburization process in which a molten iron dephosphorization step, an intermediate slag-off step, and a molten iron decarburization step are performed as a series of processes in the same converter-type vessel; prior to the molten iron dephosphorization step, the pre-charged cold iron source is charged in an amount not larger than 0.15 times a sum of an amount of the pre-charged cold iron source and a charge amount of the molten iron, or is not charged; the furnace-top-added cold iron source is added to the molten iron during one or both of the molten iron dephosphorization step and the molten iron decarburization step; and further, during at least part of a period of one or both of the molten iron dephosphorization step and the molten iron decarburization step, the powdery auxiliary material or the auxiliary material processed into powder is blown in so as to pass through a flame formed by the burner. 8 . The molten iron refining method according to claim 7 , wherein one or both of the following conditions are met: that the concentration of carbon contained in the furnace-top-added cold iron source that is added during the molten iron dephosphorization step is not lower than 0.3 mass %, and that the temperature of the molten iron upon completion of the molten iron dephosphorization step is not lower than 1380° C. 9 . The molten iron refining method according to claim 2 , wherein the refining process is a dephosphorization process of molten iron. 10 . The molten iron refining method according to claim 9 , wherein the refining process is a decarburization process that is performed with a converter-type vessel in which molten pig iron dephosphorized beforehand is charged. 11 . The molten iron refining method according to claim 2 , wherein the refining process is a dephosphorization process of molten iron. 12 . The molten iron refining method according to claim 11 , wherein one or both of the following conditions are met: that the concentration of carbon contained in the furnace-top-added cold iron source is not lower than 0.3 mass %, and that the temperature of the molten iron upon completion of the dephosphorization process is not lower than 1380° C. 13 . The molten iron refining method according to claim 2 , wherein: the refining process is a dephosphorization-decarburization process in which a molten iron dephosphorization step, an intermediate slag-off step, and a molten iron decarburization step are performed as a series of processes in the same converter-type vessel; prior to the molten iron dephosphorization step, the pre-charged cold iron source is charged in an amount not larger than 0.15 times a sum of an amount of the pre-charged cold iron source and a charge amount of the molten iron, or is not charged; the furnace-top-added cold iron source is added to the molten iron during one or both of the molten iron dephosphorization step and the molten iron decarburization step; and further, during at least part of a period of one or both of the molten iron dephosphorization step and the molten iron decarburization step, the powdery auxiliary material or the auxiliary material processed into powder is blown in so as to pass through a flame formed by the burner. 14 . The molten iron refining method according to claim 13 , wherein one or both of the following conditions are met: that the concentration of carbon contained in the furnace-top-added cold iron source that is added during the molten iron dephosphorization step is not lower than 0.3 mass %, and that the temperature of the molten iron upon completion of the molten iron dephosphorization step is not lower than 1380° C.
Blowing from above and through the bath · CPC title
Dephosphorising; Desulfurising · CPC title
Decarburising · CPC title
Blowing from above (C21C5/35 takes precedence) · CPC title
Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; {Methods of a general interest or applied to the winning of more than two metals (briquetting of scrap C22B1/248; preliminary treatment of scrap C22B1/005)} · CPC title
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