Device and method for preparing fine iron powder through suspension roasting of red mud
A technology of suspension roasting and fine iron powder, which is applied in the field of mineral processing, can solve the problems of high heat consumption, low processing capacity, low product grade and recovery rate, etc., and achieve high heat and mass transfer efficiency, recyclable waste heat, and high processing capacity big effect
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Embodiment 1
[0037] The structure of the device for preparing iron concentrate powder by suspension roasting of red mud is as follows: figure 1Shown, comprise feeding bin (1), cyclone separator (11), suspension roasting accumulator (3), burner (4), suspension roasting oxidizer (5), reducer (6), cooler ( 7) and magnetic separator (8); the discharge port of feeding bin (1) is communicated with the inlet of screw feeder (2), and the outlet of screw feeder (2) passes through pipeline and cyclone separator (11) The feed inlet at the top is communicated, the discharge outlet at the bottom of the cyclone separator (11) is communicated with the feed inlet below the suspension roasting accumulator (3), and the discharge outlet above the suspension roasting accumulator (3) is connected to the The feed port above the suspension roasting oxidizer (5) is connected, the discharge port at the bottom of the suspension roasting oxidizer (5) is connected with the feed port of the reducer (6), and the discha...
Embodiment 2
[0057] Device structure is the same as embodiment 1;
[0058] Method is with embodiment 1, and difference is:
[0059] (1) 14% by weight of water in red mud ore powder;
[0060] (2) Control the material temperature in the suspension roasting accumulator at 1000°C;
[0061] (3) Control the temperature of the solid material in the suspension roasting oxidizer at 900° C., and the residence time is 10 minutes;
[0062] (4) The residence time of the solid material in the discharge chamber is 10min, the temperature of the control material is 700°C, and the ratio of the furnace gas to the solid material in the discharge chamber is according to CO and H 2 with Fe 2 o 3 The molar ratio is 1:2;
[0063] (5) After the solid material in the reducer is reduced, it enters the cooler with the air flow, and is cooled to a temperature of 240°C through heat exchange, and then enters the magnetic separator for magnetic separation under the condition of a magnetic field strength of 2000Oe; ...
Embodiment 3
[0066] Device structure is the same as embodiment 1;
[0067] Method is with embodiment 1, and difference is:
[0068] (1) 13% by weight of water in red mud ore powder;
[0069] (2) Control the material temperature in the suspension roasting accumulator at 950°C;
[0070] (3) Control the temperature of the solid material in the suspension roasting oxidizer at 800°C, and the residence time is 20min;
[0071] (4) The residence time of the solid material in the discharge chamber is 15min, the temperature of the control material is 600°C, and the ratio of the furnace gas to the solid material in the discharge chamber is according to CO and H 2 with Fe 2 o 3 The molar ratio is 1:2;
[0072] (5) After the solid material in the reducer is reduced, it enters the cooler with the air flow, is cooled to a temperature of 220°C by heat exchange, and then enters the magnetic separator for magnetic separation under the condition of a magnetic field strength of 1000Oe;
[0073] (6) The ...
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