Method for dissolving out aluminum from pulverized fuel ash
A technology of fly ash and aluminum solution, applied in aluminum chloride, aluminum halide, alumina/aluminum hydroxide, etc., can solve the problems of high capital construction investment of pressurized dissolution equipment, low aluminum dissolution rate, and high operating cost, and achieve The effect of high aluminum dissolution rate, improving economic benefits and reducing infrastructure investment
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Embodiment 1
[0055] A circulating fluidized bed fly ash (see Table 1 for the main components) was mixed with 28% concentration of hydrochloric acid for normal pressure dissolution treatment to obtain a stripped pulp; a thickener was used to concentrate the stripped pulp to obtain the first aluminum chloride-containing The stripping liquid and concentrated pulp; the concentrated stripping pulp is mixed with 28% hydrochloric acid for pressure stripping, and oxygen (99% purity) and steam (200°C) are introduced into the stripping process; solid-liquid separation is carried out after pressurized stripping The second eluate containing aluminum chloride and the eluate slag are obtained; the first eluate and the second eluate are combined to obtain the eluate containing aluminum chloride. Among them, the solid-liquid ratio of normal pressure dissolution is 1:1.3, the normal pressure dissolution temperature is 95 degrees Celsius, the dissolution time is 2 hours, and the end point acidity is 10.3g / L;...
Embodiment 2
[0061] A circulating fluidized bed fly ash (see Table 1 for the main components) was mixed with 28% concentration of hydrochloric acid for normal pressure dissolution treatment to obtain a stripped pulp; a thickener was used to concentrate the stripped pulp to obtain the first aluminum chloride-containing The stripping liquid and concentrated pulp; the concentrated stripping pulp is mixed with 28% hydrochloric acid for pressure stripping, and oxygen (99% purity) and steam (200°C) are introduced into the stripping process; solid-liquid separation is carried out after pressurized stripping The second eluate containing aluminum chloride and the eluate slag are obtained; the first eluate and the second eluate are combined to obtain the eluate containing aluminum chloride. Among them, the solid-liquid ratio of normal pressure dissolution is 1:1.5, the normal pressure dissolution temperature is 103 degrees Celsius, the dissolution time is 3 hours, and the terminal acidity is 10.4g / L;...
Embodiment 3
[0066] A circulating fluidized bed fly ash (see Table 1 for the main components) was mixed with 28% concentration of hydrochloric acid for normal pressure dissolution treatment to obtain a stripped pulp; a thickener was used to concentrate the stripped pulp to obtain the first aluminum chloride-containing The stripping liquid and concentrated pulp; the concentrated stripping pulp is mixed with 28% hydrochloric acid for pressure stripping, and oxygen (99% purity) and steam (200°C) are introduced into the stripping process; solid-liquid separation is carried out after pressurized stripping The second eluate containing aluminum chloride and the eluate slag are obtained; the first eluate and the second eluate are combined to obtain the eluate containing aluminum chloride. Among them, the solid-liquid ratio of normal pressure dissolution is 1:1.7, the normal pressure dissolution temperature is 103 degrees Celsius, the dissolution time is 3 hours, and the terminal acidity is 14.8g / L;...
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