Preparation method for synthesizing NaX-type molecular sieve adsorption material from fly ash and application of material
An adsorption material, molecular sieve technology, applied in chemical instruments and methods, adsorption water/sewage treatment, other chemical processes, etc. The effect of recycling
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Embodiment 1
[0026] (1) The solid waste fly ash discharged from the power plant is used as raw material, dried at 100°C, and the fly ash is pretreated by adding HCl solution, wherein the liquid-solid ratio of the HCl solution to the fly ash is 10:1 (ml :g), the massfraction of HCl solution is 20%. The mixture system was stirred at 80°C for 2 hours, separated from solid and liquid, and the acidic solution in the wet precipitate was removed with deionized water, and dried to obtain the pretreated fly ash. Mix solid sodium hydroxide with pretreated fly ash at a weight ratio of 1.2:1, and roast in an open system at 550°C for 1 hour to obtain a molten product. The molten product was leached in deionized water, and stirred at a stirring speed of 400r / min for 24 hours at room temperature to obtain a silica-alumina gel, wherein the liquid-solid ratio of deionized water to the molten product was 5:1 (ml:g) . After the pH of the silica-alumina gel was adjusted to 11 with HCl solution, it was cryst...
Embodiment 2
[0030](1) Using the solid waste fly ash discharged from the power plant as the raw material, drying at 100 ° C, and pre-processing the fly ash by adding HCl solution, wherein the liquid-solid ratio of the HCl solution to the fly ash is 20:1 (ml : g), the mass fraction of the HCl solution is 10%. The mixture system was stirred at 80° C. for 3 hours, subjected to solid-liquid separation, and deionized water was used to remove the acidic solution in the wet precipitation, and dried to obtain the pretreated fly ash. The solid sodium hydroxide and the pretreated fly ash were mixed in a weight ratio of 2:1, and calcined in an open system at 550 ° C for 1.5 h to obtain a molten product. The molten product was leached in deionized water, and stirred at a stirring speed of 500 r / min for 48 hours at room temperature to obtain a silica-alumina gel, wherein the liquid-solid ratio of deionized water to the molten product was 4:1 (ml:g) . After the pH of the silica-alumina gel was adjuste...
Embodiment 3
[0034] (1) Using the solid waste fly ash discharged from the power plant as the raw material, drying at 100 ° C, and pre-processing the fly ash by adding HCl solution, wherein the liquid-solid ratio of the HCl solution to the fly ash is 15:1 (ml : g), the mass fraction of the HCl solution is 30%. The mixture system was stirred at 80°C for 2.5 hours, and after solid-liquid separation, deionized water was used to remove the acidic solution in the wet precipitation, and after drying, the pretreated fly ash was obtained. The solid sodium hydroxide and the pretreated fly ash were mixed in a weight ratio of 1.5:1, and calcined in an open system at 550 °C for 2 h to obtain a molten product. The molten product was leached in deionized water, and stirred at a stirring speed of 300 r / min for 48 hours at room temperature to obtain a silica-alumina gel, wherein the liquid-solid ratio of deionized water to the molten product was 6:1 (ml:g) . After the pH of the silica-alumina gel was adj...
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