Method for pretreating waste water containing emerging pollutants by adopting oxidation of calcium peroxide
A technology for calcium peroxide and wastewater treatment, applied in the fields of oxidized water/sewage treatment, chemical instruments and methods, precipitation treatment, etc. Toxic substance content, increase bioavailability, reduce ecotoxicity effect
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Embodiment 1
[0034] Use 20L of simulated domestic sewage, in which the simulated wastewater contains nonylphenol and triclocarban pollutants, the concentrations are 1mg / L and 1.5mg / L respectively; ammonium chloride is used to simulate the ammonia nitrogen in the sewage, and potassium dihydrogen phosphate is used to simulate the sewage Moderately soluble phosphate, the influent COD is 300mg·L -1 , TN is 30mg·L -1 , TP is 10mg·L -1 . Before the simulated wastewater enters the bioreactor, it is pretreated with calcium peroxide. The dosage of calcium peroxide is 0.5g / L, and the pH is adjusted to 8±0.1. The concentrations of phenol and triclocarban are 0.12mg / L and 0.375mg / L, indicating that calcium peroxide has degraded 88 ± 1.1% and 75 ± 0.9% of nonylphenol and triclocarban respectively. The waste water enters the biological reaction system for further reaction. By adopting the operating technical means of the present invention, the removal rate of TN in the final system effluent is 90.89±...
Embodiment 2
[0036] According to the steps and operation methods described in Example 1, domestic wastewater actually containing high-concentration estradiol pollutants was treated. The COD content in this wastewater is 150-170mg·L -1 , TN is 36.8~40.25mg·L -1 , TP is 8.7~9.6mg·L -1 , The concentration of estradiol in the wastewater is 1.5±0.87mg / L, and the influent volume of 20L of actual wastewater is also used, the dosage of calcium peroxide is 0.5g / L, and the pH is adjusted at 8±0.5. After directly entering the biological reaction system without calcium peroxide pretreatment, the concentration of nonylphenol in the effluent is 0.52±0.07mg / L, the content of nonylphenol in the sludge is 0.87±0.09mg / L, and the removal rate of TN and TP 90.2±2.3% and 92.4±0.1%, respectively. And adopt the experimental procedure of the present invention to process, experimental result is as follows: the removal rate of TN is 94.2 ± 1.5%, the removal rate of TP is 95.2 ± 3.1%, and the final effluent conce...
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