A method for reducing carbon and oxygen deposition at the end point of converter smelting
A converter smelting and terminal carbon technology, which is applied in the manufacture of converters, etc., can solve the problems of increasing the difficulty of steel purification, increasing the amount of deoxidized alloy, and increasing production costs.
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Embodiment 1
[0028]Example 1: 100T converter steelmaking, the C content of the molten iron entering the furnace is 4.5%, the temperature of the molten iron entering the furnace is 1400 ° C, the molten iron is mixed into the converter for smelting, the full oxygen supply time is 14 minutes, and the oxygen supply is added from the high-level silo when the oxygen supply is 10 minutes 110kg magnesia carbon brick and 22kg fluorite, bottom blowing argon gas flow rate is 100m 3 / h, the end temperature of the converter is 1630°C, the carbon content of molten steel is 0.05%, the oxygen content is 0.036%, and the carbon-oxygen product is 0.18*10 -6 .
Embodiment 2
[0029] Example 2: 100T converter steelmaking, the C content of the molten iron entering the furnace is 4.5%, the temperature of the molten iron entering the furnace is 1400°C, the molten iron is mixed into the converter for smelting, the full oxygen supply time is 15 minutes, and the oxygen is supplied from the high-level silo for 10.5 minutes. Add 120kg of magnesia carbon bricks and 24kg of fluorite, and the bottom blowing argon gas flow rate is 80m 3 / h, the end temperature of the converter is 1630°C, the carbon content of molten steel is 0.055%, the oxygen content is 0.04%, and the carbon-oxygen product is 0.22*10 -6 .
Embodiment 3
[0030] Example 3: 100T converter steelmaking, the C content of the molten iron entering the furnace is 4.5%, the temperature of the molten iron entering the furnace is 1400°C, the molten iron is mixed into the converter for smelting, the full oxygen supply time is 14 minutes, and the oxygen is supplied from the high-level silo for 10.5 minutes. Add 115kg of magnesia carbon bricks and 23kg of fluorite, and the bottom blowing argon gas flow rate is 90m 3 / h, the end temperature of the converter is 1630°C, the carbon content of molten steel is 0.05%, the oxygen content is 0.04%, and the carbon-oxygen product is 0.2*10 -6 .
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