Preparation method of propane dehydrogenation catalyst
A propane dehydrogenation and catalyst technology, which is applied in catalyst activation/preparation, catalysts, carbon compound catalysts, etc., can solve the problems of rapid decline in olefin selectivity, poor stability, and low dehydrogenation catalyst activity, and improve the propane dehydrogenation activity. and the effect of propylene selectivity
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preparation example Construction
[0018] There are two preparation methods of the oxidized propane dehydrogenation catalyst in the present invention, the first one is prepared by impregnation method; the second one is prepared by drop ball method.
[0019] The first preparation method of the oxidized propane dehydrogenation catalyst of the present invention comprises impregnating the alumina carrier with a manganese-containing compound solution, followed by drying and calcining.
[0020] The second preparation method of the oxidized propane dehydrogenation catalyst of the present invention comprises forming the manganese compound-containing alumina sol into balls, drying and calcining.
[0021] In the first preparation method, the alumina is preferably γ-alumina or θ-alumina. The alumina support used can be spherical, strip-shaped or clover-shaped. The temperature for impregnating alumina with manganese-containing compound solution is preferably 20-70°C, and the impregnated liquid / solid ratio is preferably 1....
example 1
[0033] The propane dehydrogenation catalyst described in the present invention is prepared.
[0034] (1) Take 0.28g of manganese acetate and dissolve it in 30ml of deionized water to make an impregnating solution, and take 20.0g of it with a specific surface area of 210m 2 / g, the pore volume is 0.5cm 3 / g γ-Al 2 o 3 Small balls, the average diameter of the small balls is 1.6 mm. The γ-Al 2 o 3 The small ball carrier is placed in the impregnation solution, stirred at 25°C for 0.5h, and left to stand for 4h for impregnation. The solid / liquid ratio of impregnation is 1.5g / ml, then dried at 120°C for 12h, and calcined at 550°C for 6h to obtain the catalyst in the oxidation state .
[0035] (2) Get the above-mentioned oxidation state catalyst, pass into propane and H 2 The mixed gas mixed at a volume ratio of 0.7:1 is subjected to reduction treatment at 580°C for 0.5h, and the mass space velocity of the mixed gas passing through the oxidized catalyst is 4.2h -1 , to obta...
example 2
[0037] Catalyst was prepared according to the method of example 1, except that the manganese acetate used in (1) step preparation impregnation solution was 0.56g, and the obtained oxidized catalyst was reduced by (2) step method to obtain catalyst B. The Mn content in Catalyst B is 1.0% by mass, and its composition is shown in Table 2.
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