Adsorption regeneration-photocatalysis advanced oxidation water treatment equipment
A technology for treating equipment and oxidizing water, which is applied in the fields of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. Improve and other problems, to achieve the effect of good catalytic reaction, large effective specific surface area, and thorough regeneration
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Embodiment 1
[0032] Embodiment 1: the working principle of the present invention is as figure 2 shown. The aeration tube 3, the ultraviolet light source 4 and the membrane module 5 are installed in the air-lift internal circulation reactor 8 to constitute the main part of the equipment of the present invention. The middle of the air-lift internal circulation reactor 8 is an upward circulation flow channel, and both sides are downward circulation flow channels, and the bottom of the downward circulation flow channel is connected to the front of the pipeline static mixer 1 through a pipeline. The membrane module 5 is connected to the water outlet pipe through a hose, and then the water is pumped out by the water outlet pump 7, and the vacuum gauge 6 is connected in series on the water outlet pipe. The powder photocatalyst 9 is suspended in the air-lift internal circulation reactor 8 . The spiral turbulence sheet 10 is placed in the water inlet pipe to form the pipeline static mixer 1 . T...
Embodiment 2
[0040] The invention is applied to the treatment of certain coking wastewater. The residence time of the reactor is 20h, the membrane module is made of polyvinylidene fluoride (PVDF), in the form of a flat membrane, and the operating flux of the membrane is 5~7 L / m 2 h, powder photocatalyst adopts Fe 2 o 3 , the dosage is 5g / L, and ozone aeration is supplemented. The influent COD concentration is 3031±571.2 mg / L, the effluent COD concentration is 303±47.2 mg / L, and the removal rate reaches 90%.
Embodiment 3
[0042] The invention is applied to the treatment of certain dye wastewater. The residence time of the reactor is 15h, the membrane module is made of polyvinylidene fluoride (PVDF), in the form of a flat membrane, and the operating flux of the membrane is 8~10 L / m 2 ·h, the powder photocatalyst uses ZnO, the dosage is 3g / L, supplemented with ozone aeration. The influent COD concentration is 1241±63.5 mg / L, the chromaticity is 230 degrees, the effluent COD concentration is 93±17.3 mg / L, the chromaticity is <20 degrees, and the removal rate reaches over 90%.
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