Advanced treatment method for wastewater produced by synthetic rubber
A technology for producing waste water and synthetic rubber, which is applied in water/sewage treatment, multi-stage water/sewage treatment, oxidized water/sewage treatment, etc. It can solve the problems of unstable operation effect and high overall cost, and achieve stable and reliable treatment effect, Low investment and easy industrial application
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Embodiment 1
[0029] The effluent from the secondary biochemical treatment of wastewater produced by a synthetic rubber factory has a pH of 6.2, a COD of 112mg / L, and a TOC of 31mg / L.
[0030] First, the wastewater is treated by catalytic oxidation, and the treatment conditions are as follows: the reaction temperature is 25°C, and the reaction pressure is normal pressure; 27.5% hydrogen peroxide is added to the wastewater, where H 2 O 2 The weight ratio of TOC to wastewater is 5.0; ferrous sulfate is added to wastewater, of which Fe 2+ With oxidant H 2 O 2 The weight ratio is 0.8; the reaction residence time is 120min. Then use 10% NaOH solution to adjust the pH of the catalytic oxidation water to 10.5, and mix and stay for 15 minutes. Then carry out slag water separation.
[0031] The COD of the water separated from the slag water is 48mg / L, and the COD removal rate is 57%; the TOC is 19mg / L, and the TOC removal rate is 39%; the total soluble iron is 0.1mg / L.
Embodiment 2
[0033] The effluent from the secondary biochemical treatment of wastewater produced by a synthetic rubber factory has a pH of 8.0, a COD of 85mg / L, and a TOC of 28mg / L.
[0034] First, the wastewater is treated by catalytic oxidation, and the treatment conditions are as follows: the reaction temperature is 50°C; the reaction pressure is normal pressure; 27.5% hydrogen peroxide is added to the wastewater, where H 2 O 2 The weight ratio of TOC to the water phase is 2.0; ferrous sulfate is added to the wastewater, of which Fe 2+ With oxidant H 2 O 2 The weight ratio is 0.4; the reaction residence time is 60min. Then use 10% NaOH solution to adjust the pH of the oxidized water to 10.0, and mix and stay for 15 minutes. Then carry out slag water separation.
[0035] The COD of the water separated from the slag water is 42mg / L, the COD removal rate is 51%; the TOC is 21mg / L, and the TOC removal rate is 25%; the total soluble iron is 0.2mg / L.
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