Method for removing organic matters in water through catalytic ozonization of FeOCl
A technology of oxyferric chloride and organic matter, applied in chemical instruments and methods, oxidized water/sewage treatment, water pollutants, etc., can solve the problems of low removal rate, high cost, long degradation time, etc., and achieve good stability , long service life, accelerated degradation and mineralization effects
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specific Embodiment approach 1
[0017] Specific embodiment one: In this embodiment, a method for catalytic ozonation of oxyferric chloride to remove organic matter in water is carried out according to the following steps:
[0018] Add water containing organic matter into the reactor, and add 2mg / L to 1000mg / L of FeOCl catalyst into the water containing organic matter under the condition of stirring speed of 300r / min~800r / min. Introduce ozone into the medium, the amount of ozone introduced is 20.5mg / L-250mg / L, and then react for 10min-40min at a temperature of 2°C-85°C to complete the catalytic ozonation of oxyferric chloride to remove organic matter in water Methods;
[0019] The molar concentration of the ozone feed amount is 5 to 50 times the molar concentration of the water body containing organic matter; the pH value of the water body containing organic matter is 1 to 13; the FeOCl catalyst is FeOCl, intercalated FeOCl or FeOCl supported on a carrier.
[0020] When the FeOCl catalyst described in this ...
specific Embodiment approach 2
[0024] Embodiment 2: The difference between this embodiment and Embodiment 1 is that the reactor is a semi-continuous flow batch columnar reactor with a cross-sectional diameter of 3 cm to 10 cm and a reactor length of 0.2 m to 2 m. The pump or magnetic circulation pump forces the water sample to circulate, and the hydraulic flow rate is 1L / h~100L / h. Others are the same as in the first embodiment.
specific Embodiment approach 3
[0025] Embodiment 3: The difference between this embodiment and Embodiment 1 or 2 is that the reactor is a continuous flow columnar reactor with a cross-sectional diameter of 2 cm to 20 cm and a reactor length of 0.5 m to 3 m. The device is filled with water from the top water tank through gravity flow, and the hydraulic flow rate is 0.5L / h~150L / h. Others are the same as in the first or second embodiment.
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