Catalyst for eliminating haloaromatic contaminant by catalytic combustion
A catalytic combustion, aromatic technology, used in physical/chemical process catalysts, catalyst carriers, chemical instruments and methods, etc., can solve problems such as loss of activity, poisoning, and reduced catalyst activity.
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example 1
[0011] TiO 2 -Al 2 o 3 Preparation of composite carrier:
[0012] Prepare a certain amount of titanium precursors such as tetrabutyl titanate, titanyl sulfate or titanium tetrachloride into ethanol or aqueous solution, and place in Al 2 o 3 Carrier, impregnated in a rotary evaporator, evaporated to dryness, hydrolyzed in the air overnight, then dried and roasted, the TiO 2 -Al 2 o 3 Composite carrier. As TiO 2 The amount of content is made into TiO with different coverage 2 -Al 2 o 3 Composite carrier. TA-0.25, TA-0.5, TA-1.0, TA-1.5 represent Al 2 o 3 TiO on support 2 The covering amounts are 4.25wt%, 8.5wt%, 17wt%, 23.5wt%, respectively.
example 2
[0014] Dissolve metal salts in water or ammonia water to prepare impregnation solution, add TiO 2 -Al 2 o 3 、Al 2 o 3 , SiO 2 、TiO 2 , CeO 2 Or honeycomb ceramics, after impregnating, drying, and roasting according to the conventional method, depending on the difference of the catalyst precursor, it is made into a single-component or two-component supported manganese-based metal oxide catalyst.
example 3
[0016] The performance evaluation of complete catalytic combustion of halogenated aromatic pollutants was carried out in an atmospheric fixed-bed quartz tube reactor. Catalyst consumption 1.0 milliliters, particle size 40-60 order, organohalogenated arene pollutant passes inert gas (such as N 2 , Ar, etc.) are bubbled into the catalyst bed (the content of chlorobenzene or dichlorobenzene is 1300ppm), the oxidant used is oxygen, and the gas space velocity is 8000h -1 . The complete catalytic combustion performance of chlorobenzene on manganese-based catalysts loaded on different supports was studied, and the test results are listed in Table 1.
[0017] Table 1 Catalytic performance of manganese-based catalysts supported on different supports for the complete combustion of chlorobenzene
[0018] Chlorobenzene conv.(%)
[0019] Catalyst Temperature(℃)
[0020] 200 250 300 350 400 450 500 550
[0021] MnO x / SiO 2 0 0 ...
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