Oxygen-enriched side-blown reduction molten pool smelting furnace and method for smelting tin by using tin-enriched complex material in smelting furnace
A molten pool smelting furnace and smelting furnace technology, applied in the field of non-ferrous metal smelting, can solve the problems of high energy consumption, low processing capacity, and unorganized emission of smoke in electric furnaces, and achieve the effect of improving economic benefits
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Examples
Embodiment 1
[0035] The tin-rich material contains Sn40%, Pb3%, FeO22%, add 15% reduced coal, and mix with quartz stone according to the silicic acidity of the slag of 0.9, and make 10~40mm pellets by the granulator, and send them to the oxygen-enriched side blowing Reduction bath smelting furnace; O is fed into the primary tuyere 2 Oxygen-enriched air with a concentration of 50%, the pressure of the primary tuyere is 0.16Mpa, the wind speed is 250m / s, the bituminous coal is adjusted, and the value of the oxygen excess coefficient α is controlled to be 0.6~0.7 in the feeding stage, 0.4~0.5 in the reducing stage, and 0.8~0.9 in the discharging stage ; Fully burn the bituminous coal, heat the melt and keep the melt temperature at 1250°C, control the reducing atmosphere in the melting pool of the smelting furnace, make the tin oxide reduction reaction for 55 minutes, and generate coarse tin, slag and smoke; send the liquid slag into the oxygen-enriched tin Fuming furnace, through O 2 Oxygen-...
Embodiment 2
[0037] The tin-rich material contains Sn30%, Pb13%, FeO26%, add 18% reduced coal and quartz stone to mix according to the silicic acidity of slag 0.8, and make 10~40mm pellets by granulator, and send them into oxygen-enriched side blowing reduction Melting pool melting furnace; O is fed into the primary tuyeres 2 Oxygen-enriched air with a concentration of 25%, the pressure of the primary tuyere is 0.08Mpa, the wind speed is 150m / s, the bituminous coal is adjusted, and the value of the oxygen excess coefficient α is controlled to be 0.55~0.65 in the feeding stage, 0.35~0.5 in the reducing stage, and 0.8~0.9 in the discharging stage ; Fully burn the bituminous coal, heat the melt and keep the melt temperature at 1050°C, control the reducing atmosphere in the molten pool of the smelting furnace, make the tin oxide reduction reaction for 45 minutes, and generate crude tin, slag and smoke; send the liquid slag into the oxygen-enriched tin Fuming furnace, through O 2 Oxygen-enrich...
Embodiment 3
[0039] The tin-rich material contains Sn25%, Pb18%, FeO27%. Add 20% reduced coal and quartz stone to mix according to the silicic acidity of the slag to 1.0, and make 10~40mm pellets by the granulator, and send them to the oxygen-enriched side blown reduction Melting pool melting furnace; O is fed into the primary tuyeres 2 Oxygen-enriched air with a concentration of 35%, primary tuyere pressure of 0.14Mpa, wind speed of 200m / s, adjusting bituminous coal, and controlling the oxygen excess coefficient α value in the feeding stage 0.55~0.65, reducing stage 0.35~0.5, and discharging stage 0.8~0.9 , to fully burn the bituminous coal, heat the melt and keep the melt temperature at 1150°C, control the reducing atmosphere in the melting pool of the smelting furnace, make the tin oxide reduction reaction for 50 minutes, and generate coarse tin, slag and smoke; send the liquid slag into the oxygen-enriched tin Fuming furnace, through O 2 Oxygen-enriched air with a concentration of 25%...
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Description
Claims
Application Information
- IPC
- C22B25/02
- Inventors
- 李果; 谢官华



