Catalytic ozonation treatment method for refining sewage
A technology for refining and chemical sewage and ozone oxidation, which is applied in the fields of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. It can solve problems such as the reduction of catalytic activity, reduce consumption and meet environmental protection standards. , to achieve the effect of deep processing
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Embodiment 1
[0035] According to the technical process provided by the present invention, the oily sewage air flotation water (COD 869.3mg / L) of a certain refinery is processed, and the main processing unit process conditions are as follows: the amount of coal-based powdered activated carbon added to A pool is 60mg / L; A / O tank residence time is 8 / 20h, COD load is 0.8kg COD / m 3 d, the sludge concentration is 5g / L, the sludge internal return ratio is 300%, the sludge external return ratio is 100%, and the aeration intensity of the aerobic tank is 7m 3 / m 2 h, the hydraulic retention time of the secondary sedimentation tank is 1.0h; the sand filter uses quartz sand as the filler, and the filtration rate is 6m / h; the catalytic ozonation tower is filled with coal-based powdered activated carbon loaded with copper oxide and iron oxide, and the hydraulic retention time The ozone dosage is 40mg / L; the ozone concentration is 50mg / L; the residence time of the intermediate pool is 1.0h; the biologic...
Embodiment 2
[0038] According to the technical process provided by the present invention, the saline sewage air flotation effluent (COD 1257.2mg / L) of a certain refinery is processed, and the main processing unit process conditions are as follows: the amount of wood-based powdered activated carbon added to pool A is 80mg / L ; A / O tank residence time is 12 / 24h, COD load is 1.0kg COD / m 3 d, sludge concentration 6g / L, sludge internal reflux ratio 300%, sludge external reflux ratio 100%, aerobic tank aeration intensity 8m 3 / m 2 h, the hydraulic retention time of the secondary sedimentation tank is 1.5h; the sand filter uses wood-based granular activated carbon as filler, and the filtration rate is 5m / h; the catalytic ozonation tower is filled with cerium oxide granular activated carbon, and the hydraulic retention time is 1.0h; The dosage of ozone is 50mg / L; the concentration of ozone is 80mg / L; the residence time of the middle pool is 0.5h; the filler of the biological aerated filter is cera...
Embodiment 3
[0041] According to the technical process provided by the present invention, the oily sewage air flotation water (COD 869.3mg / L) of a certain refinery is processed, and the main processing unit process conditions are as follows: the amount of coconut shell-based powdered activated carbon added to the A pool is 40mg / L ; A / O tank residence time is 6 / 12h, COD load is 0.3kg COD / m 3 d, sludge concentration 2g / L, sludge internal reflux ratio 200%, sludge external reflux ratio 80%, aerobic tank aeration intensity 5m 3 / m 2 h, the hydraulic retention time of the secondary sedimentation tank is 0.5h; the sand filter uses anthracite as filler, and the filtration rate is 5m / h; the catalytic ozonation tower is filled with coconut shell-based granular activated carbon, and the hydraulic retention time is 1.5h; the dosage of ozone The ozone concentration is 20mg / L; the residence time of the middle pool is 1.5h; the biological aerated filter is filled with zeolite, the filtration rate is 2m...
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