Application of mesoporous alumina loaded magnetic ferroferric oxide nano material to catalytic ozonation
A mesoporous alumina and catalyst technology, which is applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, oxidized water/sewage treatment, etc., can solve solid-liquid separation, serious metal dissolution, Poor effect and other problems
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specific Embodiment approach 1
[0011] Specific implementation mode one: Fe 3 o 4 / Al 2 o 3 Catalyst preparation
[0012] A certain amount of Fe(NO 3 ) 3 9H 2 O was dissolved in a small amount of deionized water, a certain amount of mesoporous alumina carrier was added to it, impregnated for 2 hours, then dried at 100°C, and calcined at 400-500°C for 3-6 hours in an air atmosphere to obtain Fe 2 o 3 / Al 2 o 3 . Fe 2 o 3 / Al 2 o 3 in H 2 Reduction at 250-350°C for 2-4 hours under atmosphere to obtain Fe 3 o 4 / Al 2 o 3 , where Fe 3 o 4 The mass content is 10-50wt%.
specific Embodiment approach 2
[0013] Specific implementation mode two: Fe 3 o 4 / Al 2 o 3 Catalytic ozonation activity of the catalyst
[0014] In a 1L columnar bubbling semi-continuous reactor, 2,4-dichlorophenoxyacetic acid was used as the target pollutant to evaluate Fe according to the present invention 3 o 4 / Al 2 o 3 catalytic ozonation activity. The reaction temperature is 25°C, pH=6, the gas flow rate of the ozone-oxygen mixed gas is 0.2L / min, the ozone concentration in the gas is 30mg / L, and the catalyst dosage is 1g / L.
[0015] figure 1 When pH=6,2,4-dichlorophenoxyacetic acid initial concentration is 20mg / L, Fe 3 o 4 / Al 2 o 3 Removal of TOC by 2,4-dichlorophenoxyacetic acid as a function of time. As can be seen from the figure, when pH=6, the removal effect of single ozone oxidation on 2,4-dichlorophenoxyacetic acid is not obvious (the removal rate of TOC in 20 minutes is 32%), adding Fe 3 o 4 20 minutes after the catalyst, the TOC removal rate reached 60%, while the addition of ...
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