A method for the treatment and recycling of mixed acid wastewater in the photovoltaic industry
A recycling method and recycling technology, which is applied in the field of mixed acid wastewater treatment and resource recycling in the photovoltaic industry, can solve the problem of low removal efficiency, achieve the effects of improving fluorine removal efficiency, reducing foam formation, and improving treatment efficiency
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Embodiment 1
[0037] figure 1 It is a simple process flow diagram of the present invention, combined with figure 1 , the method for the treatment and recycling of mixed acid wastewater in the photovoltaic industry of this embodiment includes the following steps:
[0038] a) In this embodiment, the molar concentration of fluoride ions in the mixed acid wastewater in the photovoltaic industry is 0.637mol / L, and the molar concentration of nitrate nitrogen is 0.04mol / L. The first fluoride removal pool and the second fluoride removal pool;
[0039] B) add calcium hydroxide emulsion in the first defluoridation pond, the molar concentration of calcium ion in the calcium hydroxide emulsion is 30% of the fluoride ion molar concentration in the first defluorination pond, i.e. the molar concentration of calcium ion is 0.191mol / L, the pH value of the first defluoridation tank is 4.0, so that fluoride ions and calcium ions form calcium fluoride precipitation, and the mud-water mixture in the first def...
Embodiment 2
[0045] The treatment and recycling method of mixed acid wastewater in the photovoltaic industry of this embodiment includes the following steps:
[0046] a) In this example, the molar concentration of fluoride ions in the mixed acid wastewater in the photovoltaic industry is 0.342 mol / L, and the molar concentration of nitrate nitrogen is 0.064 mol / L. The above wastewater is introduced into the regulating tank for water quality homogenization, and the volume ratio is 3:1. The first fluoride removal pool and the second fluoride removal pool;
[0047] B) add calcium hydroxide emulsion in the first defluoridation pond, the molar concentration of calcium ion in the calcium hydroxide emulsion is 40% of the fluoride ion molar concentration in the first defluorination pond, i.e. the molar concentration of calcium ion is 0.137mol / L, the pH value of the first defluoridation tank is 6.0, so that fluoride ions and calcium ions form calcium fluoride precipitation, and the muddy water mixtu...
Embodiment 3
[0053] The treatment and resource recycling method of mixed acid wastewater in the photovoltaic industry in this embodiment, the operation steps are as follows:
[0054] a) In this example, the molar concentration of fluoride ions in the mixed acid wastewater of the photovoltaic industry is 1.158mol / L, and the molar concentration of nitrate nitrogen is 0.086mol / L. The first fluoride removal pool and the second fluoride removal pool;
[0055] B) add calcium hydroxide emulsion in the first defluoridation pond, the molar concentration of calcium ion in the calcium hydroxide emulsion is 35% of the fluoride ion molar concentration in the first defluorination pond, i.e. the molar concentration of calcium ion is 0.405mol / L, the pH value of the first defluoridation tank is 5.2, so that fluoride ions and calcium ions form calcium fluoride precipitation, and the muddy water mixture in the first defluoridation tank is introduced into the second defluoridation tank;
[0056] c) measure t...
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