Process for treating used water difficult to degradate by catalytic internal electrolysis of iron
A technology of internal electrolysis and catalytic iron, which is applied in the direction of chemical instruments and methods, water/sewage treatment, water/sewage multi-stage treatment, etc., can solve the problems of iron filings agglomeration, failure to operate, and decline in effect, and achieve treatment costs Inexpensive, improved processing effect and speed, powerful effect
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Embodiment 1
[0017] Example 1: Comparison of the effects of the method of the present invention and the prior art in treating wastewater.
[0018] The first step: weigh three parts of iron filings with the same weight. The first part is pure iron filings without adding catalyst copper and modified zeolite, called filter media A; the second part is adding catalyst copper, iron filings and copper filings Press W Cu / W Fe =0.6 ratio, fully mixed to form filter material B; the third part is based on the second part and 3% cationic surfactant modified zeolite of the total amount of iron filings and copper filings is added, fully mixed to form filter media C. Three filter materials A, B and C are put into three filter tanks respectively. The following implementation steps are the same.
[0019] Step 2: Adjust the pH of the wastewater in the filter to 8.5, let the wastewater circulate in the filter with a reflux ratio of 5:1 at room temperature without aeration, and the hydraulic retention time is 1....
Embodiment 2
[0023] Example 2: Using the method of the present invention to treat gasoline wastewater.
[0024] Step 1: Press W on the copper and iron sheets Cu / W Fe =0.5 The proportion is well weighed, and 3% of the total weight of the copper flakes and the iron flakes are added to the cationic surfactant modified zeolite, and the filter material is fully mixed and placed into the filter tank.
[0025] The second step: adjust the pH of the wastewater to 8.0, let the wastewater circulate in the filter tank with a reflux ratio of 6:1 at room temperature without aeration, and the hydraulic retention time is 1 hour to make the wastewater fully react in the filter tank.
[0026] The third step: stand still for 30 minutes and measure the supernatant. The results are shown in Table 2.
[0027] Wastewater
Embodiment 3
[0028] Example 3: Treatment of wastewater in a chemical industry zone by the method of the present invention
[0029] Step 1: Press W on the copper and iron sheets Cu / W Fe =0.4 The proportion is well weighed, and 3% of the total weight of copper flakes and iron flakes are added with cationic surfactant-modified zeolite, mixed thoroughly, and put into the filter tank.
[0030] Step 2: Adjust the pH of the wastewater to 7.5, and let the wastewater circulate in the filter tank with a reflux ratio of 6:1 at room temperature without aeration. The hydraulic retention time is 2 hours to make the wastewater fully react in the filter tank.
[0031] The third step: after refluxing, adjust the pH to 8.5, settle for 30 minutes, and measure the supernatant (see Table 3).
[0032] Waste water
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