Integrated mechanical photocatalytic membrane separation coupling reactor and wastewater treatment method thereof
A photocatalytic membrane and mechanical technology, which is applied in the field of integrated mechanical photocatalytic membrane separation coupling reactor and its wastewater treatment, can solve the problems of short membrane life, difficult separation of photocatalyst, complicated structure of photocatalytic membrane device, etc. Achieve the effect of low production cost, low energy consumption and high efficiency
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Embodiment 1
[0024] figure 1 It is the view of the integrated mechanical photocatalytic membrane separation coupling reactor of the present invention, figure 2 It is a top view of the integrated mechanical photocatalytic membrane separation coupling reactor of the present invention. Such as figure 1 and figure 2 As shown, the integrated mechanical photocatalytic membrane separation coupling reactor is provided with a water inlet zone 1, a mixing zone 2, a reaction zone 3 and a water outlet zone 4. The mixing zone 2 and the reaction zone 3 are columnar containers respectively, the lower ends of the side walls of the two are flush, and the relative positions of the mixing zone 2, the reaction zone 3 and the water outlet zone 4 are in the shape of concentric sleeves arranged sequentially from inside to outside. The water inlet zone 1 is a tubular structure lying under the mixing zone 2 , the reaction zone 3 and the water outlet zone 4 .
[0025] The water inlet 1 is provided with a wate...
Embodiment 2
[0030] The integrated mechanical photocatalytic membrane separation coupling reactor of Example 1 is used to process coking wastewater. The initial COD value of coking wastewater is 163.5mg / L, and the TOC value is 12mg / L. The treatment conditions are as follows:
[0031] Processing time: 60min;
[0032] Photocatalyst dosage: 2.5g / L;
[0033] The COD value in the treated wastewater is 70.3mg / L, and the TOC value is 2.8mg / L;
[0034] In addition, ordinary photocatalytic process equipment is used to treat coking wastewater. The initial COD value of coking wastewater is 163.5mg / L, TOC value is 12mg / L, the experimental conditions (treatment time and photocatalyst dosage) are exactly the same, and the COD value after treatment is 98.8mg / L. The TOC value is 3.9mg / L.
Embodiment 3
[0036] Use the integrated mechanical photocatalytic membrane separation coupling reactor of embodiment 1 to process commercial humic acid and prepare water to be treated, COD value 89.8mg / L, TOC value 8.7mg / L, process under the following conditions:
[0037] Processing time: 40min;
[0038] Photocatalyst dosage: 1.5mg / L;
[0039] After treatment, the COD value is 38.6mg / L, and the TOC value is 1.6mg / L;
[0040] In addition, ordinary photocatalytic process equipment is used to process commercial humic acid to prepare water to be treated. The COD value is 89.8mg / L, the TOC value is 8.7mg / L, the experimental conditions (treatment time and photocatalyst dosage) are exactly the same, and the COD value after treatment is 49.1mg. / L, TOC value 2.9mg / L.
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