A method for treating phenolic wastewater
A technology for phenolic wastewater and wastewater, which is applied in the field of treating phenolic wastewater, can solve the problems that phenolic wastewater cannot meet the treatment requirements, and achieve the effects of low cost, less material, and simple operation
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specific Embodiment approach 1
[0024] The water sample is phenol cyanide coking wastewater, COD=5120mg / L, volatile phenol=298mg / L.
[0025] Experiment 1: Determining Polymerized AlCl 3 Dosage, take 5 waste water samples, each 500mL, the measured pH value is 6-7, respectively add the polymerized AlCl with a mass concentration of 10% 3 Solution, the dosage is 5mL, 6mL, 7mL, 8mL, 9mL, stir evenly, then add 40mL polyacrylamide solution with a mass concentration of 0.1% as a coagulant, stir evenly, let stand for 20min, observe 5 water samples of. Add 5 mL of polymerized AlCl 3 The precipitated flocs of the sample were in small pieces, the supernatant was turbid, and the interstitial water was turbid, indicating that the amount of polyacrylamide added was appropriate, while the polymerization of AlCl 3 The amount of addition is not enough; add 6mL polymerized AlCl 3 The precipitated flocs of the samples were in the form of small pieces, the supernatant was clear, and the interstitial water was relatively clea...
specific Embodiment approach 2
[0030] Compared with the specific embodiment one, adding H in 3 times 2 o 2 , add 2mL H every 15min 2 o 2 . After the secondary flocculation is completed, COD=350mg / L, volatile phenol=7.8mg / L, and the total removal rate of COD and volatile phenol is about 93.2% and 97.4% respectively. h 2 o 2 The effect of multiple dosing is better than that of single dosing.
[0031] Take the supernatant and adsorb with activated carbon for about 1 h at room temperature. At this time COD≈140mg / L, volatile phenol=3mg / L. At this time, the total removal rate of COD is about 97.5%, and the total removal rate of volatile phenol is about 98.9%, which is a light yellow transparent liquid. It has reached the national secondary standard for comprehensive sewage discharge.
specific Embodiment approach 3
[0033] Compared with the second embodiment, after adjusting the pH of the water sample to 4-6, first add zero-valent iron iron flakes to react for about 20 minutes, and then add H in 3 times 2 o 2 , Reaction 0.5 ~ 1h. After the secondary flocculation, the measured COD=310mg / L, volatile phenol=6.2mg / L. It shows that appropriately increasing the reaction time of zero-valent iron can increase the treatment of organic matter.
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