Method for producing industrial activated aluminum oxide from pulverized fuel ash
A technology of activated alumina and fly ash, applied in the removal of alumina/aluminum hydroxide, solid waste, etc., can solve the problems of corrosion of metal equipment by hydrochloric acid, high energy and resource consumption, complex process, etc. Utilize the effect of significant benefit, large energy consumption and resource consumption, and simple operation steps
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Embodiment 1
[0043] Embodiment 1: raw material fly ash is composed of: Al 2 o 3 Content 37.7%, Fe 2 o 3 Content 4.38%, CaO content 3.74%, MgO content 0.54%, SiO 2 The content is 49.9%, and the loss on ignition is 1.92%. The raw fly ash can also use other components and their corresponding amounts.
[0044] Mill the fly ash in a ball mill for 1 hour for mechanical activation; add water according to the mass ratio of fly ash to water 1:3, stir well, and remove unburned black through flotation, which can be used to make carbon black or directly burn Produce heat; remove iron oxide by magnetic separation, and the obtained impurity magnetite powder is used to produce cement, make iron black pigment or ironmaking; combine the fly ash residue after flotation carbon and magnetic separation with concentrated sulfuric acid Prepare a mixed solution with a mass concentration of sulfuric acid of 40%, control the solid-to-liquid ratio (mass ratio) of fly ash to the mixed solution to 1:8, heat and pre...
Embodiment 2
[0046] Example 2: The fly ash used in Example 1 was ball milled in a ball mill for 2 hours to perform mechanical activation; water was added according to the mass ratio of fly ash to water of 1:3, fully stirred, and unburned net was removed by flotation black; then remove iron oxide by magnetic separation; make a mixed solution with a sulfuric acid concentration of 50% from the fly ash residue after flotation carbon and magnetic iron separation and concentrated sulfuric acid, and control the solid-liquid concentration of fly ash and the mixed solution The ratio is 1:7, and the heating and pressurizing reaction is carried out in the acid-resistant reaction equipment for 4 hours. The maximum temperature of the reaction is 240°C and the pressure is 0.1MPa; after the reaction cools down, add water according to the mass ratio of fly ash to water at 1:15, After heating and boiling, the filter cake was obtained by suction filtration, and washed with water with a mass ratio of fly ash ...
Embodiment 3
[0049] Example 3: The fly ash in Example 1 was ball milled in a ball mill for 3 hours to perform mechanical activation; according to the mass ratio of fly ash and water of 1:2, water was added, fully stirred, and unburned net was removed by flotation black; then remove iron oxide by magnetic separation; make a mixed solution with a sulfuric acid concentration of 80% from the fly ash residue after flotation carbon and magnetic iron separation and concentrated sulfuric acid, and control the solid-liquid concentration of fly ash and the mixed solution The ratio is 1:6, and the heating and pressurizing reaction is carried out in the acid-resistant reaction equipment for 5 hours. The maximum temperature of the reaction is 240°C and the pressure is 0.2MPa; after the reaction cools down, add water according to the mass ratio of fly ash to water at 1:10, After heating and boiling, the filter cake was obtained by suction filtration, and washed with water with a mass ratio of fly ash to ...
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