A kind of preparation method of gamma-alumina carrier with high specific surface area
A high specific surface area, alumina carrier technology, applied in catalyst carriers, chemical instruments and methods, catalyst activation/preparation, etc., can solve the problems of bad, influence, and high calcination temperature, and achieve low calcination temperature, simple preparation process, no cost. easily destroyed effect
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[0008] Preparation method of the present invention:
[0009] First, weigh a certain amount of pseudo-boehmite powder, physical pore-enlarging agent and extrusion aid, and add them to the kneader to mix evenly. During the mixing process, add the aqueous solution of peptizer evenly, and knead to the best plastic state. , and then extruded into clover-shaped strips (diameter 1mm), cut into small pieces of 1cm, dried naturally at room temperature, and then dried in a constant temperature blast drying oven at 100°C, and the dried molding was added to the rotary kiln After multi-stage constant temperature roasting, γ-alumina is finally produced.
[0010] The specific surface area of the pseudo-boehmite powder described in the method of the present invention≧250m 2 / g, pore volume 0.7-0.9mL / g. The physical pore-enlarging agent is fumed white carbon black. The amount of the physical pore-enlarging agent added is 1% to 3% of the weight of the pseudo-boehmite powder, preferably...
Embodiment 1
[0015] Weigh pseudo-boehmite powder (specific surface area≧250m 2 / g, pore volume 0.7-0.9mL / g) 1000g, add 10g of meteorological silica, 10g of fennel powder and mix evenly, dissolve 3.3g of nitric acid and 6.7g in 10g of deionized water, and mix the obtained solution with the above materials Evenly, knead to the best plastic state, then extrude into 3mm clover-shaped strips on a hydraulic extruder, cut into 1cm pieces, dry at room temperature for 12h, and then dry at 100°C for 10h. The dried molded product was placed in a tubular rotary furnace, and fired at 170°C for 1h, 310°C for 1h, 360°C for 1h, and 550°C for 1h. The alumina carrier A1 provided by the present invention is obtained.
Embodiment 2
[0017] The same as in Example 1, except that the addition amount of fumed silica powder is 20 g, the addition amount of squash powder is 20 g, and other conditions remain unchanged, and the alumina carrier A2 provided by the present invention is obtained.
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