Method for Extracting Chromium and Vanadium from Vanadium-Chrome Iron Water and Reducing Oxygen Consumption
A technology of vanadium chromium molten iron and oxygen, which is applied in the manufacture of converters, etc., can solve the problems of difficult extraction of chromium, and achieve the effects of overcoming low conversion temperature of carbon and chromium, reducing carbon oxidation rate, and simple process
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Embodiment 1
[0036] After the 80t converter is finished adding iron, the oxygen lance is lowered in place, and 30% coolant is added after successful ignition. The coolant is iron oxide or coolant containing iron oxide. After blowing for 1.5 minutes, add 20% coolant. The last 50% of the coolant is added 2 minutes before the blowing is stopped, and the oxygen blowing time is controlled at 9 minutes; the oxygen pressure of the converter is 0.65MPa, and the flow rate is controlled at 8000Nm 3 / h, oxygen consumption is 15Nm 3 / tFe; the amount of coolant is controlled at 30kg / tFe; the flow rate of bottom nitrogen gas in the non-converting stage is controlled at 0.002m 3 / (min·tFe) or less, use 0.12m from blowing to 1.5min before the end of blowing 3 / (min·tFe) intensity bottom blowing CO 2 Gas, the bottom blowing gas is switched to nitrogen 1.5 minutes before the end of blowing to start the next furnace; after the end of smelting, the semi-steel and vanadium-chromium slag are separated, and th...
Embodiment 2
[0038] After the 200t converter is finished adding iron, the oxygen lance is lowered in place, and 10% coolant is added after successful ignition. The coolant is iron oxide or coolant containing iron oxide. After blowing for 1.5 minutes, 50% coolant is added. The last 40% of the coolant is added 2 minutes before the blowing is stopped, and the oxygen blowing time is controlled at 12 minutes; the oxygen pressure of the converter is 1.0MPa, and the flow rate is controlled at 24000Nm 3 / h, oxygen consumption is 35Nm 3 / tFe; the amount of coolant is controlled at 60kg / tFe; the flow rate of bottom nitrogen gas in the non-converting stage is controlled at 0.002m 3 / (min·tFe) or less, use 0.60m from blowing to 1 minute before the end of blowing 3 / (min·tFe) intensity bottom blowing CO 2 Gas, the bottom blowing gas is switched to nitrogen gas 1 minute before the end of blowing to start the next furnace; after the end of smelting, the semi-steel and vanadium-chromium slag are separat...
Embodiment 3
[0040] After the 140t of iron mixing is completed, the oxygen lance is lowered into place and 20% of the coolant is added after successful ignition. 40% of the coolant is added 2 minutes before the blowing is stopped, and the oxygen blowing time is controlled at 10 minutes; according to the capacity of the converter, the oxygen pressure is 0.85MPa and the flow rate is controlled at 16000Nm 3 / h, oxygen consumption is 20Nm 3 / tFe; the amount of coolant is controlled at 45kg / tFe; the flow rate of bottom nitrogen gas in the non-converting stage is controlled at 0.002m 3 / (min·tFe) or less, use 0.40m from blowing to 1.5min before the end of blowing 3 / (min·tFe) intensity bottom blowing CO 2 Gas, the bottom blowing gas is switched to nitrogen 1.5 minutes before the end of blowing to start the next furnace; after the end of smelting, the semi-steel and vanadium-chromium slag are separated, and the obtained semi-steel is transported to the steelmaking converter for steelmaking. Va...
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