Method for oxygen-enriched side-blowing direct reduction smelting of anode mud
A technology of anode slime and lead anode slime, which is applied in the direction of improving process efficiency, etc., can solve problems such as difficult to achieve multi-parameter, multi-process, and effective control, and achieve the effects of reducing equipment investment, low energy consumption, and large processing capacity
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Embodiment 1
[0026] See attached figure 1 , figure 1 Be the structural representation of the side-blowing furnace that the present invention utilizes, among the figure 1 is a smoke outlet, 2 is a charging port, 3 is an air inlet, 4 is a heating device, 5 is a slag outlet, and 6 is a lead outlet.
[0027] The side-blowing furnace is a circular shaft furnace, the upper part of the side-blowing furnace is provided with a smoke outlet 1, the middle and upper part of the right side of the side-blowing furnace is provided with a feeding port 2 and an air inlet 3 in turn, and the lower part of the right side is provided with a heating device 4; A slag outlet 5 and a lead outlet 6 are provided at the middle and lower part on the left side of the side-blowing furnace.
[0028] The method for direct reduction smelting of oxygen-enriched side-blown anode slime of the present invention, the detailed steps of the method are as follows:
[0029] a. First, add the slagging agent soda ash and reducing...
Embodiment 2
[0032] Embodiment 2: basically the same as Embodiment 1, the difference is:
[0033] In step a: the dry weight of the lead anode slime, the slagging agent soda ash and the reducing agent coke particles are added in a weight ratio of 100:6:10;
[0034] In step b: the mixed material obtained in step a is continuously added to the side blowing furnace at a speed of 9t / h from the feed port 2 of the side blowing furnace; the addition of oxygen-enriched gas is 230Nm 3 / h, the amount of gas added is 310Nm 3 / h; the temperature in the side-blowing furnace is controlled by the DSC system to be 1000°C.
Embodiment 3
[0035] Embodiment 3: basically the same as Embodiment 1, the difference is:
[0036] In step a: the dry weight of the lead anode slime, the slagging agent soda ash and the reducing agent coke particles are added in a weight ratio of 100:3:5;
[0037]In step b: the mixed material obtained in step a is continuously added to the side blowing furnace from the feed port 2 of the side blowing furnace at a speed of 7t / h; the addition of oxygen-enriched gas is 250Nm 3 / h, the amount of gas added is 330Nm 3 / h; the temperature in the side-blowing furnace is controlled by the DSC system to be 1200°C.
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