Device and method for extracting iron from iron tailings through suspension roasting
A suspension roasting and suspension roasting furnace technology is applied in the directions of cyclone devices, chemical instruments and methods, magnetic separation, etc., which can solve the problems of low efficiency and poor production continuity.
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Embodiment 1
[0063] The structure of the device for iron tailings suspension roasting and iron extraction is as follows: figure 1 As shown, it includes a feeding bin 2, a Venturi dryer 5, a first cyclone preheater 6, a second cyclone preheater 7, a pre-oxidation suspension roaster 8, a heat separation cyclone 10, a suspension reduction roaster 12, Collection bin 18, dry magnetic separator 19, first stage grinding machine 20, first stage weak magnetic separator 21, second stage grinding machine 22, second stage weak magnetic separator 23, dust collector 26 and induced draft fan 30;
[0064] A feeding belt 1 is provided above the feeding bin 2 for transferring materials to the feeding bin 2; a loss-in-weight feeder 3 is arranged between the feeding bin 2 and the screw feeder 4, and the loss-in-weight feeder 3 is connected with the screw feeder 4 respectively. The outlet of the feeding bin 2 is opposite to the feeding end of the screw feeder 4, and the feeding port of the screw feeder 4 is op...
Embodiment 2
[0091] Device structure is the same as embodiment 1;
[0092] The iron tailings used are flotation iron tailings, iron grade TFe 19.24%, containing SiO by mass percentage 2 47%, method is the same as embodiment 1, and difference is:
[0093] (1) Crushing and grinding the iron tailings to a particle size of -0.038mm accounts for 60% of the total mass;
[0094] (2) Control the temperature of the material at the outlet of the Venturi dryer 5 to be 135°C; the solid material is preheated to 450°C in the second cyclone preheater 7;
[0095] (3) The pre-oxidation roasting temperature is 680°C; the residence time of the material entering the pre-oxidation roaster in the pre-oxidation roaster is 15min;
[0096] (4) The reduction roasting temperature is 580°C; 2 / CO and Fe in oxide slag powder 2 o 3 1.2 times the amount required for complete reaction theory; control the volume concentration of gas in the pre-oxidation roaster to 30%; the residence time of pre-oxidation slag powder...
Embodiment 3
[0100] Device structure is the same as embodiment 1;
[0101] The iron grade of the iron tailings used is TFe 15.86%, containing SiO by mass percentage 2 45%, method is the same as embodiment 1, and difference is:
[0102] (1) Crushing and grinding the iron tailings to a particle size of -0.038mm accounts for 70% of the total mass;
[0103] (2) Control the temperature of the material at the outlet of the Venturi dryer 5 to be 140°C; the solid material is preheated to 500°C in the second cyclone preheater 7;
[0104] (3) The pre-oxidation roasting temperature is 700°C; the residence time of the material entering the pre-oxidation roaster in the pre-oxidation roaster is 10min;
[0105] (4) The reduction roasting temperature is 600°C; 2 / CO and Fe in oxide slag powder 2 o 3 1.3 times the amount required for complete reaction theory; control the volume concentration of gas in the pre-oxidation roaster to 20%; the residence time of pre-oxidation slag powder in the reduction r...
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