Method for industrial production of polymeric aluminum ferric chloride water purification agent with coal ash
A technology of polyaluminum chloride and iron water purifier, applied in the direction of flocculation/sedimentation water/sewage treatment, etc., can solve the problems of high production cost of calcium aluminate powder, unfavorable industrialization implementation, long production line, etc., and achieve the extension of coal The effect of industrial chain, low cost and low production cost
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Embodiment 1
[0016] Embodiment 1: As shown in Figure 1, a kind of method that utilizes fly ash industrial production water purifying agent-polyaluminum ferric chloride, 20 tons of fly ash is added to reactor, and injection mass percentage is 10% at the same time 30 tons of industrial waste hydrochloric acid, add 0.5 tons of sodium chloride in parts by weight, and fully stir in the reactor, the reactor is sealed to prevent acid volatilization. Inject steam for heating, heat to 80°C-95°C, and react for 1 hour until a qualified feed liquid is obtained, wherein the qualified feed liquid: the mass fraction of alumina is 10.4%, the mass fraction of iron oxide is 1.5%, and the water-insoluble The mass fraction is 0.44%, the basicity is 45, and the density is 1.19g / cm 3 , PH=3.5. Among them, the qualified feed liquid is put into the clarification tank for solid-liquid separation, and the supernatant and the coal ash waste slag of powder polyaluminum ferric chloride are separated, the separated su...
Embodiment 2
[0017] Embodiment 2: as shown in Figure 2, a kind of method that utilizes fly ash industrial production water purifying agent-polyaluminum ferric chloride, 30 tons of fly ash is added to reactor, and injection mass percentage is 20% at the same time 48 tons of industrial hydrochloric acid, add 0.1 tons of potassium chloride, and fully stir in the reactor, seal the reactor to prevent acid volatilization. Inject steam for heating, heat to 90°C-100°C, and react for 2 hours to obtain a qualified feed liquid, wherein the qualified feed liquid: the mass fraction of alumina is 11%, the mass fraction of iron oxide is 1.6%, and the content of water-insoluble The mass fraction is 0.35%, the basicity is 60, and the density is 1.20g / cm 3 , pH=5.0. Among them, put the qualified feed liquid into the clarification tank for solid-liquid separation, separate the supernatant and fly ash waste residue, inject the separated supernatant into the polymerization kettle, add 1 ton of sodium carbonat...
Embodiment 3
[0018] Embodiment 3: as shown in Figure 2, a kind of method that utilizes fly ash industrial production water purifying agent-polyaluminium ferric chloride, 25 tons of fly ash is added to reactor, injecting mass percentage simultaneously is 10% 48 tons of industrial waste hydrochloric acid, add 0.5 tons of calcium chloride, and fully stir in the reactor, seal the reactor to prevent acid volatilization. Inject steam for heating, heat to 95°C-105°C, and react for 3 hours until a qualified feed liquid is obtained, wherein the qualified feed liquid: the mass fraction of alumina is 11%, the mass fraction of iron oxide is 1.9%, and the water-insoluble The mass fraction is 0.34%, the basicity is 65.8, and the density is 1.22g / cm 3 , pH=4.5. Among them, put the qualified feed liquid into the clarification tank for solid-liquid separation, separate the supernatant and fly ash waste residue, inject the separated supernatant into the polymerization kettle, add 1.4 tons of calcium hydrox...
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