Method for producing aluminum oxide from high-alumina fly ash
A high-aluminum fly ash and alumina technology, applied in the removal of alumina/aluminum hydroxide, solid waste, etc., can solve the problem of high energy consumption for aluminum salt concentration crystallization and pyrolysis, low alumina product purity, and sintering materials. It can reduce the consumption of reducing agent, improve the utilization rate of acid, and reduce energy consumption.
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Embodiment 1
[0038] Take 100g fly ash, according to Al in fly ash 2 o 3 Take 95% sulfuric acid at 3.5 times the number of moles, and mix it with fly ash for 3 times. After adding acid and mixing well, acidolyze and solidify at 150°C. Sulphate and roast at 320°C for 2 hours, mix the obtained sulfated calcined sand with coal powder at a coal ratio of 8%, and then reduce and roast at 750°C for 7 minutes to obtain the reduced calcined sand.
[0039] Alkali leaching is carried out on the reduced calcine, and the dissolution conditions are: dissolution temperature 100°C, alkali concentration 50g / L, ingredient molecular ratio α k 0.9, time 60min, lime addition 0%. The leaching rate of the obtained aluminum is 85%. The leaching liquid is desiliconized and seeded to obtain an aluminum hydroxide product, which is calcined to prepare a metallurgical grade alumina product, and the seeded mother liquor is returned to the reduced calcined sand for dissolution.
Embodiment 2
[0041] Take 100g fly ash, according to Al in fly ash 2 o 3 Take sulfuric acid with a concentration of 93% which is 4 times the number of moles, and mix it with fly ash in 2 times. After adding acid and mixing well, acidolyze and solidify at 200°C. After the last batch of sulfuric acid is added and mixed well, heat up Sulphate and roast at 320°C for 2 hours, mix the obtained sulfated calcined sand with coal powder at a coal ratio of 10%, and then reduce and roast at 750°C for 7 minutes to obtain the reduced calcined sand.
[0042] Alkali leaching is carried out on the reduced calcine, and the dissolution conditions are: dissolution temperature 90°C, alkali concentration 100g / L, ingredient molecular ratio α k 1.2, time 60min, lime addition 2%. The leaching rate of the obtained aluminum is 89%. The leaching liquid is desiliconized and seeded to obtain aluminum hydroxide products, which are calcined to prepare metallurgical grade alumina products, and the seeded mother liquor i...
Embodiment 3
[0044] Take 100g fly ash, according to Al in fly ash 2 o 3 Take 93% sulfuric acid at 4.5 times the number of moles, and mix it with fly ash in 3 times. After adding acid and mixing well, acidolyze and solidify at 200°C. Sulphate and roast at 350°C for 2 hours, mix the obtained sulfated calcined sand with coal powder at a coal ratio of 10%, and then reduce and roast at 750°C for 7 minutes to obtain the reduced calcined sand.
[0045] Alkali leaching is carried out on the reduced calcine, and the dissolution conditions are: dissolution temperature 150°C, alkali concentration 100g / L, ingredient molecular ratio α k 1.2, time 60min, lime addition 2%. The leaching rate of the obtained aluminum is 90%. The leaching solution is desiliconized and seeded to obtain an aluminum hydroxide product, which is calcined to prepare a metallurgical grade alumina product, and the seeded mother liquor is returned to the reduced calcined sand for dissolution.
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