Method for producing alumina by using high-alumina fly ash
A high-alumina fly ash and alumina technology, applied in the direction of alumina/aluminum hydroxide, can solve the problems of large slag phase flow in the ammonium sulfate sintering method, difficult industrial production of metallurgical-grade alumina, and low recovery rate, and achieve Reduce equipment cost and operation difficulty, good industrialization scalability, and save production cost
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Embodiment 1
[0041] 1) Pre-desiliconization, after heating the mixed solution composed of high-aluminum fly ash and 20% sodium hydroxide solution (the mass ratio of sodium hydroxide to high-alumina fly ash is 0.5:1) to 110°C, Import into a pressure vessel for desiliconization reaction for 2 hours, and then carry out liquid-solid separation to obtain liquid-phase desiliconization liquid and solid-phase fly ash filter cake. The aluminum-silicon ratio in the fly ash filter cake is higher than that before the desilication reaction. High fly ash; the mass content of alumina in high aluminum fly ash is higher than 40%;
[0042] 2) Preparation of raw slurry: add fly ash filter cake to the slurry made of limestone and sodium carbonate to obtain mixed slurry, grind the mixed slurry in a ball mill and prepare raw slurry; before mixing quicklime and sodium carbonate, After grinding, the calcium ratio of the raw slurry is 2, the alkali ratio is 1, and the moisture content is 30wt%;
[0043] 3) Clinke...
Embodiment 2
[0055] 1) Pre-desilication, heating the mixed solution composed of high alumina fly ash and 10% sodium hydroxide solution (the mass ratio of sodium hydroxide solution to high alumina fly ash is 0.6:1) to 130°C , introduced into the insulation retention tank for desiliconization reaction for 2.5h, and then liquid-solid separation was carried out after the evaporator was decompressed to obtain the desiliconization liquid in the liquid phase and the desiliconization fly ash filter cake in the solid phase, wherein the aluminum of the original fly ash The silicon ratio is 1.15, which rises to 2.12 after desiliconization, and the SiO in the desiliconization solution 2 The concentration is 62g / l;
[0056] 2) Preparation of raw slurry, adding fly ash filter cake to a slurry made of limestone (quicklime) and sodium carbonate to obtain a mixed slurry, grinding the mixed slurry in a ball mill and blending into a raw slurry; limestone and sodium carbonate Grinding is required before mixi...
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