Method for removing organic pollutant in water by catalysis ozonation
A technology for removing organic pollutants and water, applied in water pollutants, oxidized water/sewage treatment, chemical instruments and methods, etc., can solve problems such as secondary pollution of water bodies, human health effects, etc., to reduce toxicity and reduce bromic acid Salt formation, effect of overcoming the influence of oxidation efficiency
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specific Embodiment approach 1
[0009] Specific embodiment one: the method for catalytic ozonation of this embodiment to remove organic pollutants in water is realized by the following steps: a, in the form of a fluidized bed or a fixed bed, a solid catalyst with a particle size of 1 nm to 10 cm is put into the ozone catalytic oxidation contact reaction In the reactor, the total thickness of the solid catalyst is controlled at 10-500cm; b. The water to be treated is introduced into the reactor in a downstream, counter-current or mixed manner at a water flow rate of 1-50m / h, before the reactor or The reactor adopts titanium plate microporous aeration, standpipe aeration or surrounding uniform aeration to carry out ozone distribution. Add hydrogen peroxide at a molar ratio of 1:0.1~1; c. Control the contact time between ozone, hydrogen peroxide and water to be treated at 1 to 300 minutes, and contact the catalyst with water to be treated containing ozone and hydrogen peroxide The time is 1 to 180 minutes, that...
specific Embodiment approach 2
[0010] Embodiment 2: The difference between this embodiment and Embodiment 1 is that the reactor in step a adopts a tubular type, an oxidation tank or an oxidation tower. Other steps and parameters are the same as those in Embodiment 1.
specific Embodiment approach 3
[0011] Specific embodiment three: the difference between this embodiment and specific embodiment one is that the solid catalyst in step a is arranged continuously, segmented or layered; wherein segmental arrangement is adopted in the tubular or oxidation pool reactor, each segment The length is 1-100cm, and the middle interval is 1-100cm; in the oxidation tower reactor, it is arranged in layers, and the thickness of each layer is 1-100cm, and the middle interval is 1-100cm. Other steps and parameters are the same as those in Embodiment 1.
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