Preparation method of wastewater remediation agent based on incineration fly ash
A technology for incinerating fly ash and repairing agents, which is applied in chemical instruments and methods, water pollutants, water/sewage treatment, etc. It can solve the problems of high disposal cost, low removal rate, secondary pollution, etc., and achieves a simple preparation method, The effect of cheap raw materials and efficient removal
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Embodiment 1
[0019] Effects of incineration fly ash, tuff powder and sodium hydroxide mass ratio on the removal of hexavalent chromium, pentavalent arsenic, divalent cadmium and benzo(α)pyrene in water:
[0020] Such as figure 1 Shown, is the preparation process of waste water remediation agent, specifically: according to incineration fly ash, tuff powder, sodium hydroxide mass ratio is 10:0.5:0.1, 10:1:0.25, 10:1.5:0.5, 10:1.5: 1. 10:2:1, 10:4:1, 10:4:1.5, 10:4:2, 10:6:1, 10:6:1.5, 10:6:2, 10:8:1, 10:8:1.5, 10:8:2, 10:10:2, 10:10:2.5, 10:10:3, 10:11:3, 10:12:3, weigh incineration fly Ash, tuff powder and sodium hydroxide were mixed evenly, and then activated at 300°C for 2 hours to obtain activated fly ash powder; according to the mass ratio of iron tailings and scrap iron slag as 4:1, weigh iron tailings and Scrap iron slag, mix evenly, grind at high speed for 1 hour, cross 100 mesh sieves, obtain iron base powder; Ash powder, iron-based powder, and sodium peroxodisulfate are mixed ev...
Embodiment 2
[0027] Effect of activated fly ash powder activation temperature on the removal of hexavalent chromium, pentavalent arsenic, divalent cadmium and benzo(α)pyrene in water:
[0028] According to the mass ratio of incineration fly ash, tuff powder, and sodium hydroxide as 10:6:2, weigh the corresponding mass of incineration fly ash, tuff powder, and sodium hydroxide, mix them evenly, and then heat them at 100°C, 150°C, and 200°C respectively. ℃, 250°C, 280°C, 300°C, 400°C, 500°C, 600°C, 700°C, 800°C, 900°C, 920°C, 950°C, 1000°C for 5 hours to obtain activated fly ash powder; The mass ratio of iron tailings and waste iron slag is 3:1, take iron tailings and waste iron slag respectively, mix uniformly, grind at high speed for 2.5 hours, cross 200 mesh sieves, obtain iron-based powder; press activated fly ash powder, The mass ratio of iron-based powder and sodium peroxodisulfate is 10:2:2. The activated fly ash powder, iron-based powder and sodium peroxodisulfate are weighed respect...
Embodiment 3
[0034] The effect of the mass ratio of iron tailings and scrap iron slag on the removal of hexavalent chromium, pentavalent arsenic, divalent cadmium and benzo(α)pyrene in water:
[0035] According to the mass ratio of incineration fly ash, tuff powder and sodium hydroxide as 10:6:2, weigh the corresponding mass of incineration fly ash, tuff powder and sodium hydroxide, mix them evenly, and then activate them at 700°C for 8 hours. The activated fly ash powder is obtained; the mass ratio of iron tailings and waste iron slag is 5:1, 4.5:1, 4.2:1, 4:1, 3.5:1, 3:1, 2.5:1, 2:1, 1.5:1, 1:1, 0.8:1, 0.5:1, 0.2:1, respectively weigh iron tailings and scrap iron slag, mix evenly, grind at high speed for 4 hours, and pass through a 300-mesh sieve to obtain iron-based powder; The mass ratio of activated fly ash powder, iron-based powder, and sodium peroxodisulfate is 10:3:3. Weigh the activated fly ash powder, iron-based powder, and sodium peroxodisulfate respectively, mix them evenly, an...
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