Wastewater treatment method based on ta, al co-doped iron oxide photocatalyst
A technology for iron oxide light and wastewater treatment, applied in the field of photocatalysis, can solve the problems of high cost, catalyst doping with many precious metals, etc.
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Embodiment 1
[0063] The wastewater to be treated in this embodiment is mixed wastewater containing Cr(VI) and phenol, wherein the initial concentration of phenol is 10 mg / l, and the initial concentration of Cr(VI) is 10 mg / l.
[0064] The wastewater treatment method based on the Ta, Al co-doped iron oxide photocatalyst of the present embodiment, the treatment process is as follows:
[0065] S1: Adjust the pH value of the wastewater to be treated to 3; the method for adjusting the pH is as follows:
[0066] by dropwise addition of 1M H 2 SO 4 solution or 1M NaOH solution to adjust the pH value of the simulated wastewater.
[0067] S2: After the pH value is adjusted, the photocatalytic treatment is carried out. The photopositive electrode in the photocatalytic electrode pair used in the photocatalytic treatment includes a conductive substrate and a Ta and Al co-doped iron oxide photocatalyst film coated on the surface of the conductive substrate. , the cathode is a titanium sheet.
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Embodiment 2
[0085] The same treatment method as in Example 1 is used to treat different waste water, that is, the photoanode electrode, the treatment process and the parameters of each step are the same when carrying out waste water treatment. The difference is that in the waste water to be treated, Cr(VI) and The initial concentration of phenol was varied.
[0086] The initial concentrations of Cr(VI) and phenol in the waste water to be treated in the present embodiment are as follows:
[0087] The initial concentration of Cr(VI) was 10 mg / l, and the concentration of phenol was 10 mg / l, 20 mg / l, 30 mg / l, and 40 mg / l, respectively.
[0088] figure 2 For wastewater treatment based on Ta and Al co-doped iron oxide photocatalysts, the synergistic degradation of the wastewater to be treated is respectively under the condition of different phenol concentrations.
[0089] Depend on figure 2 It can be seen that increasing the phenol concentration from 10mg / l to 30mg / l will promote the degra...
Embodiment 3
[0091] Same as Example 1, the difference is that the processing conditions are different. In this embodiment, it is carried out under the conditions of pure electricity and pure light respectively.
[0092] Research on Ta / Al-Fe 2 o 3 Synergistic degradation of Cr(VI) and phenol by catalytic film under different light conditions.
[0093] Figure 3a and Figure 3b are the degradation rates of Cr(VI) and phenol in the wastewater to be treated under pure electric conditions (EC), pure light conditions (PC) and photoelectric synergistic conditions (PEC), where the corresponding The curve is the same as in Example 1.
[0094] Depend on Figure 3a It can be seen that the degradation effect of Cr(VI) under the condition of photoelectric synergy is significantly better than that of pure light and pure electricity. Due to Fe 2 o 3 Thin films are visible light-based catalysts, which are better under pure light than pure electricity conditions. Depend on Figure 3b It can be s...
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