Method for regulating multistage-cascade induction electro-Fenton by graded addition of H2O2 on basis of pH indication
A technology of H2O2 and induction electricity, applied in the direction of sterilization/microdynamic water/sewage treatment, etc., can solve the problems of lack of scientific basis, decreased treatment efficiency of Fenton technology, waste of input materials, etc., to optimize implementation parameters and save engineering. The effect of implementing cost and improving utilization efficiency
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Embodiment 1
[0034] Wastewater from an enterprise (COD about 315mg / L, pH about 6.5) such as figure 1 As shown, the three-stage homogeneous induction electro-Fenton process is adopted, and the residence time of the designed reactor is 30min. H 2 o 2 Concentration C 1 Adjust to 0.02mol / L, pH 0 After being adjusted to 3, it passes through the first-stage induction electric Fenton reactor and then enters the second and third-stage reactors in turn. After connecting the external power supply and running stably for 30 minutes, the pH 0 to pH 3 They were 3, 4.2, 5.3 and 6.5 respectively, and the COD value of the effluent was 235mg / L, which did not meet the third-level standard for wastewater discharge (COD is less than or equal to 100mg / L). found to meet the pH 0 +11 2 n Conditions, take measures 1 to make the following adjustments: At the same time, add H 2 o 2 , such that C 1 0.04mol / L, C 2 0.03mol / L, C 3 It is 0.02mol / L. After adjusting and running for 30 minutes, the pH 0 to pH ...
Embodiment 2
[0038] A chemical factory produces biochemical effluent (COD value is about 450mg / L, pH is about 6.6) using such as figure 2 The shown 4-stage homogeneous induction electro-Fenton process treatment, the design reactor residence time is 20min, the influent pH 0 Adjust to 3, and add H at the same time before the 4th grade reactor 2 o 2 , so that C 1 to C 4 The concentration is 1mol / L. After connecting the external power supply and running stably for 20 minutes, the pH 1 to pH 4 They were 3, 4.1, 5.2, 5.9 and 6.6 in turn, and the COD value of the final effluent was reduced to 180mg / L, but it still did not meet the emission requirements. found to meet the pH 0 +11 2 n Conditions, take measures 1 to adjust as follows: at the same time, adjust the H 2 o 2 Dosage, so that C 11.5mol / L, C 2 1.5mol / L, C 3 1.5mol / L and C 4 It is 1.5mol / L. After adjusting and running for 20 minutes, the COD value of the effluent is 88mg / L, and the pH 0 to pH 3 They are 3, 3.3, 3.6 and 3.9...
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