Method for synchronously removing heavy metals and organic matters from wastewater
A technology for organic matter and heavy metals, applied in chemical instruments and methods, water pollutants, water/sewage treatment, etc., to achieve the effects of improving degradation efficiency, mild reaction conditions, and reducing chemical dosage
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Embodiment 1
[0038] Take a certain electroplating wastewater, pH=6.3, the initial concentration and removal rate of pollutants in this water sample are shown in Table 1.
[0039] (1) Anoxic reaction: take 1L of the industrial wastewater, add FeSO to it 4 ·7H 2 O 2.78g, then the molar concentration of Fe is 10mmol / L. The sum of the molar concentrations M of heavy metal ions in the wastewater is 4.0mmol / L, then the molar ratio of Fe to M is 2.5:1, which meets the technical characteristics of greater than 2:1; the COD concentration in the wastewater is 120mg / L, and the Fe mass concentration and COD concentration The ratio is 4.7:1, which meets the technical characteristics of greater than 3:1. Add the adjusted wastewater to the anoxic tank, control the dissolved oxygen concentration of the wastewater to less than 1.0 mg / L, adjust the pH to 7.0, and react for 10 minutes to generate FeM catalyst with high activity in situ.
[0040] (2) Incubation reaction: After the reaction in the anoxic ta...
Embodiment 2
[0046] Take a certain electroplating wastewater, pH=2.1, the initial concentration and removal rate of pollutants in this water sample are shown in Table 2.
[0047] (1) Anoxic reaction: take 1L of the industrial wastewater, add FeSO to it 4 ·7H 2 O 3.34g, then the molar concentration of Fe is 12mmol / L. The total molar concentration M of heavy metal ions in the wastewater is 4.7mmol / L, then the molar ratio of Fe to M is 2.5:1, which meets the technical characteristics of greater than 2:1; the COD concentration in the wastewater is 60mg / L, and the Fe mass concentration and COD concentration The ratio is 11.2:1, which meets the technical characteristics of greater than 3:1. Add the adjusted wastewater to the anoxic tank, control the dissolved oxygen concentration of the wastewater to less than 1.0 mg / L, adjust the pH to 7.0, and react for 20 minutes to generate FeM catalyst with high activity in situ.
[0048] (2) Incubation reaction: After the reaction in the anoxic tank, th...
Embodiment 3
[0054] Take a certain titanium dioxide production wastewater, pH = 1.2, the initial concentration and removal rate of pollutants in this water sample are shown in Table 3.
[0055] (1) Anoxic reaction: Take 1L of this industrial wastewater, because the mass concentration of Fe in the wastewater is 3148mg / L, that is, the molar concentration is 56mmol / L. And the molar concentration sum M of heavy metal ions in the waste water is 2.1mmol / L, then the molar ratio of Fe and M is 26.2:1, accords with the technical feature greater than 2:1; COD concentration is 447mg / L in the waste water, Fe mass concentration and COD The concentration ratio is 7.0:1, which meets the technical characteristics of greater than 3:1, so Fe ions are no longer added to the wastewater. Add the adjusted wastewater to the anoxic tank, control the dissolved oxygen concentration of the wastewater to less than 1.0 mg / L, adjust the pH to 7.0, and react for 30 minutes to generate FeM catalyst with high activity in ...
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