Method of extracting silica gel from high-alumina fly ash
A high-alumina fly ash and silica gel technology, applied in the direction of silicon oxide, silicon dioxide, etc., can solve the problems of reducing reaction rate, difficult control, and restricting application, so as to reduce environmental pollution, scientific and reasonable process design, and high reaction rate fast effect
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Embodiment 1
[0023] This embodiment provides a method for extracting silica gel from high-alumina fly ash, the method comprising the following steps:
[0024] 1) High alumina fly ash (among them, SiO 2 and Al 2 o 3 The mass percentages are 41% and 45%, respectively) and the aqueous solution containing sodium sulfate and aluminum sulfate (wherein, the content of sodium sulfate is 150g / L, and the content of aluminum sulfate is 250g / L) according to the solid-liquid ratio of 1:4 Mixing and preparing to make raw slurry;
[0025] 2) Sinter the raw slurry obtained above at a temperature of 1000°C for 2.5 hours to make clinker; at the same time, it is accompanied by SO 3 generation, the SO produced by this step 3 It can be sent to the next step after being absorbed by sulfuric acid with a mass fraction of 10-40%, which is used for the acid dissolution of clinker;
[0026] 3) The sulfuric acid with a mass fraction of 5% and the clinker obtained above were reacted at 60° C. for 30 min at a mass...
Embodiment 2
[0029] This embodiment provides a method for extracting silica gel from high-alumina fly ash, the method comprising the following steps:
[0030] 1) High alumina fly ash (among them, SiO 2 and Al 2 o 3 The mass percentages are 43% and 50%, respectively) and the aqueous solution containing sodium sulfate and aluminum sulfate (wherein, the content of sodium sulfate is 200g / L, and the content of aluminum sulfate is 300g / L) according to the solid-liquid ratio of 1:3.5 Mixing and preparing to make raw slurry;
[0031] 2) Sinter the raw slurry obtained above at a temperature of 1200°C for 1.5 hours to make clinker; at the same time, it is accompanied by SO 3 generation, the SO produced by this step 3 It can be sent to the next step after being absorbed by sulfuric acid with a mass fraction of 10-40%, which is used for the acid dissolution of clinker;
[0032] 3) The sulfuric acid with a mass fraction of 10% and the clinker obtained above were reacted at 80° C. for 20 minutes at...
Embodiment 3
[0035] This embodiment provides a method for extracting silica gel from high-alumina fly ash, the method comprising the following steps:
[0036] 1) High alumina fly ash (among them, SiO 2 and Al 2 o 3 The mass percentages are 41% and 51%, respectively) and the aqueous solution containing sodium sulfate and aluminum sulfate (wherein, the content of sodium sulfate is 260g / L, and the content of aluminum sulfate is 450g / L) according to the solid-liquid ratio of 1:3 Mixing and preparing to make raw slurry;
[0037] 2) Sinter the raw slurry obtained above at a temperature of 1300°C for 0.5h to make clinker; at the same time, it is accompanied by SO 3 generation, the SO produced by this step 3 It can be sent to the next step after being absorbed by sulfuric acid with a mass fraction of 10-40%, which is used for the acid dissolution of clinker;
[0038] 3) React 10 min of sulfuric acid with a mass fraction of 15% and the clinker obtained above at 95°C in a mass ratio of 5:1, fil...
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