Method for treating sewage through catalytic oxidation
A technology for catalytic oxidation and wastewater treatment, which is applied in the direction of oxidized water/sewage treatment, chemical instruments and methods, multi-stage water/sewage treatment, etc. It can solve problems affecting the effect of catalytic oxidation reactions, achieve good social benefits, and reduce consumption , cost reduction effect
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Embodiment 1
[0032] To treat the biochemical effluent of an oil refinery, H 2 o 2 as an oxidizing agent, Fe 2 SO 4 as a catalyst, ethylenediaminetetraacetic acid as a complexing agent, and the acid-base used is concentrated H 2 SO 4 and NaOH. The operating conditions are determined as: H 2 o 2 / Wastewater COD mass concentration ratio 1:4, H 2 o 2 with Fe 2+ The molar concentration ratio is 2:1, complexing agent and Fe 2+ The molar ratio is 1:1; the pH of the oxidation reaction tank is 5, the pH of the sedimentation tank is 6.5, the residence time of the oxidation reaction tank is 30 minutes, and the residence time of the sedimentation tank is 1 hour. See Table 1 for the data comparison between the catalytic oxidation treatment method of the present invention and the traditional catalytic oxidation treatment method for wastewater treatment. The results in Table 1 show that waste residue and catalyst consumption are significantly reduced by adopting the method of the present inven...
Embodiment 2
[0037] To treat high-concentration wastewater from a chemical plant, H 2 o 2 as an oxidizing agent, Fe 2 SO 4 as a catalyst, oxalic acid as a complexing agent, and the acid-base used is concentrated H 2 SO 4 and NaOH. The operating conditions are determined as: H 2 o 2 / COD mass concentration ratio of wastewater 1:8, H 2 o 2 with Fe 2+ The molar concentration ratio is 1:1, complexing agent and Fe 2+ The mol ratio is 1: 2; the pH of the oxidation reaction tank is 6, the pH of the sedimentation tank is 6.5, the residence time of the oxidation reaction tank is 40 minutes, and the residence time of the sedimentation tank is 1 hour, adopting the catalytic oxidation treatment method of the present invention and the traditional catalytic oxidation treatment See Table 2 for the data comparison of wastewater treated by the method. The results in Table 2 show that waste residue and catalyst consumption are significantly reduced by adopting the method of the present invention...
Embodiment 3
[0042] Treatment of saline wastewater from a factory, using sodium hypochlorite as oxidant, Fe 2 SO 4 As a catalyst, citric acid is a complexing agent, and the acid-base used is concentrated H 2 SO 4 and NaOH. The operating conditions are determined as: H 2 o 2 The mass concentration ratio of COD / wastewater is 1:5, the oxidant and Fe2+ The molar concentration ratio is 3:1; complexing agent and Fe 2+ The mol ratio is 1: 2; the pH of the oxidation reaction tank is 4, and the pH of the sedimentation tank is 6.5; the residence time of the oxidation reaction tank is 30 minutes, and the residence time of the sedimentation tank is 1 hour, using the catalytic oxidation treatment method of the present invention and the traditional catalytic oxidation treatment See Table 3 for the data comparison of wastewater treated by the method. The results in Table 3 show that waste residue and catalyst consumption are significantly reduced by adopting the method of the present invention to t...
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