Method for reducing pyrolusite and co-producing sulfuric acid by utilizing sulfur in fluidized bed furnace
A technology of fluidized bed furnace and pyrolusite, which is applied in the direction of manganese sulfate, chemical instruments and methods, sulfur compounds, etc., can solve the problems of high labor intensity, long process, and environmental pollution, and achieve reduced equipment investment, good operating conditions, and large economic benefits Effect
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Embodiment 1
[0023] Mix sulfur and pyrolusite into the fluidized furnace in a ratio of 1:3, and blow air into the lower part of the fluidized furnace to make the material boil and burn in the fluidized furnace under the action of the furnace bottom airflow and the negative pressure on the furnace top to control the boiling layer. At a temperature of 850-950°C, the sulfur mixed in the pyrolusite burns to generate sulfur dioxide, which generates a lot of heat; the sulfur and the produced sulfur dioxide reduce the manganese dioxide in the pyrolusite to manganese monoxide. The manganese monoxide discharged from the discharge port of the fluidized fluidized furnace falls into the water to isolate the air for cooling to prevent the manganese monoxide from being oxidized into manganese dioxide, and the manganese monoxide can also be directly discharged into the sulfuric acid solution (or electrolytic manganese anolyte) for slurrying and leaching manganese sulfate . The furnace gas in the lower se...
Embodiment 2
[0025] Carry out embodiment 1 repeatedly by above-mentioned same procedure, sulfur and pyrolusite are mixed in ratio 1: 7 and send in the fluidized furnace, control boiling layer temperature 800-900 ℃, fluidized furnace outlet temperature 800-900 ℃, the concentration of sulfur dioxide at the fluidized furnace outlet is 10-12%.
Embodiment 3
[0027] Carry out embodiment 1 repeatedly by above-mentioned same procedure, sulfur and pyrolusite are mixed in ratio 1: 15 and sent in the fluidized furnace, control boiling layer temperature 750-850 ℃, fluidized furnace outlet temperature 800-850 ℃, the concentration of sulfur dioxide at the fluidized furnace outlet is 8-10%.
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