Preparation of Co3O4 / CeO2 composite oxide and catalytic application
A composite oxide and catalyst technology, applied in metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, chemical/physical process, etc., can solve the problem of large influence on catalytic activity
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Embodiment 1
[0010] Co with an atomic ratio of cobalt to cerium of 19 to 1 3 o 4 / CeO 2 Preparation of composite oxides. Preparation of Co with an atomic ratio of cobalt to cerium of 19 to 1 by precipitation oxidation 3 o 4 / CeO 2 composite oxide catalyst. Under stirring conditions at 333K, 1 mol / L Co(NO 3 ) 2 ·6H 2 O and 1 mol / L Ce(NO 3 ) 3 ·6H 2 O aqueous solution was slowly dropped into 0.2 mol / L sodium carbonate aqueous solution in proportion, the pH value was adjusted to 10.0 with 0.2 mol / L NaOH, and after aging at this temperature for 4 h, it was filtered and washed with deionized water. Then, the obtained precipitate was mixed again with deionized water and stirred, and an appropriate amount of H 2 o 2 (30%). After aging for 1 h, it was filtered and washed with deionized water again, dried at 383 K for 12 h, and calcined at 538 K for 4 h.
Embodiment 2
[0012] Co with an atomic ratio of cobalt to cerium of 19 to 1 3 o 4 / CeO 2 Test of performance of composite oxide catalysts in catalytic oxidation reaction of carbon monoxide. The activity test of the catalyst was carried out in a miniature fixed-bed quartz tube reactor at atmospheric pressure. The composite oxide powder was pressed into tablets, crushed and sieved to 40-60 mesh, and 200 mg was packed in a Ф=6 mm quartz reaction tube. Reagent gas CO / O 2 / He=1 % / 21 % / He, the total gas flow rate is 50 ml / min. The low temperature reaction is to immerse the U-shaped reactor in the liquid nitrogen container, and control the reaction temperature by adjusting the distance between the catalyst and the liquid nitrogen surface. The humidity condition was achieved by bubbling the reaction gas through a 298 K constant temperature water bath (moisture content was 3.1 vol%). Before the reaction, the catalyst was pretreated in air at 538 K for 1 h. The gas at the outlet of the reactor...
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