Carbon reducing, sulfur reducing, iron removing and iron ore concentrate recovering method for coal ash
A technology for fly ash and iron recovery, applied in the field of solid waste resource utilization
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Embodiment 1
[0026] (1) Loss on ignition 9.0%, SO 3 The content of 9.6% fluidized bed boiler electrostatic precipitator fly ash was reduced and roasted at 900°C for 15 minutes.
[0027] (2) Quickly pour the fly ash after reduction and roasting into the water quenching tank for water quenching cooling. The bottom of the water quenching tank is provided with a fly ash slurry discharge valve, and the water quenching tank is equipped with a stirrer to break up the sintered lumps ; The notch is provided with a fishing net or a scraper to collect floating carbon on the water surface.
[0028] (3) Use a wet weak magnetic separator to magnetically separate iron concentrate from the fly ash slurry cooled by water quenching, with a magnetic field strength of 170mT. The iron concentrate and tailings are subjected to suction filtration and drying respectively to obtain iron concentrate and magnetic separation ash.
[0029] (4) The iron ore concentrate with a yield of 8.3% and a TFe grade of 52.9% wa...
Embodiment 2
[0031] (1) The fly ash of the fluidized bed boiler electrostatic precipitator with 9.0% loss on ignition and 9.6% SO3 content was reduced and roasted at 900°C for 30 minutes.
[0032] (2) Same as step (2) of Example 1.
[0033] (3) Same as step (3) of Example 1.
[0034](4) The iron ore concentrate with a yield of 8.9% and a TFe grade of 47.9% was finally obtained, and the recovery rate of total iron was 48.6%. 3 content dropped to 0.34%.
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