Carrier of silver catalyst for olefin epoxidation as well as preparation method and application thereof
A technology of silver catalyst and alumina carrier, which is applied in the direction of catalyst carrier, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve the problem of reducing the rate of decline in catalyst selectivity and achieve selectivity Improved effect
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[0055] Example 1
[0056] a) Preparation of the carrier
[0057] Alpha-trihydrate Al with 50-500 mesh and heavy alkaline earth metal content of 28 ppm (by mass) 2 O 3 312g, more than 200 mesh, the content of heavy alkaline earth metal is 227ppm (by mass) pseudomonohydrate Al 2 O 3 92g, NH 4 7g of F was put into a mixer and mixed evenly, transferred to a kneader, added with 0.12 liter of dilute nitric acid (nitric acid: water = 1:3, weight ratio), and kneaded into an extrudable paste. It is extruded into a five-hole column with an outer diameter of 8.0 mm, a length of 6.0 mm and an inner diameter of 1.0 mm, and is dried at 80-120° C. for more than 2 hours to reduce the free water content to less than 10%.
[0058] Put the above-mentioned five-hole column into a bell jar kiln, raise the temperature from room temperature to 1400° C. for about 30 hours, and keep the constant temperature for 4 hours to obtain white α-Al 2 O 3 carrier sample. The measured carrier performan...
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[0071] Example 2
[0072] The same as in Example 1, the difference is that 61 g of petroleum coke was added during the preparation of the carrier. See Table 1 for carrier data. The silver catalyst data and catalytic performance data are shown in Table 2.
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[0077] Example 3
[0078] With the embodiment 1, the difference is that the use of heavy alkaline earth metal content is 490ppm α-trihydrate Al 2 O 3 212g, pseudomonohydrate Al with heavy alkaline earth metal content of 52ppm 2 O3 192g and adding Vaseline 10g, NH 4 F7g; the five-hole column was kept constant for 12h from room temperature to 1230°C; 2.8g of strontium acetate was added instead of 3.6g of barium acetate, 0.3g of lithium sulfate and 0.6g of perrhenic acid when preparing the dipping solution; after dipping The carrier was heated at 220 °C. The data of the prepared carrier is shown in Table 1; the silver catalyst data and catalytic performance data are shown in Table 2.
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