Catalyst for producing olefins from synthesis gas and preparation method thereof
A catalyst and synthesis gas technology, which is applied in the field of high activity and stability loaded iron-based synthesis gas to low-carbon olefin catalysts and its preparation, can solve the problems of low-carbon olefin catalyst activity and stability need to be further improved, high catalyst cost, CO conversion Low efficiency and other problems, to achieve the effect of outstanding comprehensive performance, improved conversion rate, and improved selectivity
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example 1
[0025] Weigh commercially available alumina (pore volume is 0.96ml / g, specific surface area is 286.81m 2 / g, saturated water absorption is 145ml / g, provided by Sinopec Catalyst Co., Ltd. Fushun branch, the following examples and comparative examples all use the alumina), the sucrose mass concentration is 5% aqueous solution with sulfuric acid to adjust the pH value equal to 3. Immediately after the saturated spraying and impregnating alumina, dry at 95°C for 1 hour, the adsorption amount of the acidic solution for drying sugar is 60% of the saturated absorption solution of the alumina carrier, aging at 60°C for 7 hours, and drying at 100°C 24 hours, and then calcined at 300° C. for 5 hours to obtain a modified alumina carrier. The above-mentioned modified alumina carrier was impregnated with an aqueous zinc nitrate solution with a mass fraction of 5% by unsaturated spray impregnation method, the immersion temperature was 50°C, the immersion time was 3h, the impregnation amount ...
example 2
[0028] Weigh commercially available alumina, adjust the pH value of the aqueous solution with a sucrose mass concentration of 20% to 1 with sulfuric acid, and immediately dry at 110°C for 0.5h after saturated spraying and impregnating the alumina to reach the adsorption capacity of the acidic solution of sugar. It is 40% of the saturated absorption solution of the alumina carrier, aged at 80°C for 4 hours, dried at 120°C for 8 hours, and then calcined at 400°C for 3 hours to obtain a modified alumina carrier. The above-mentioned modified alumina carrier is impregnated with an aqueous solution of zinc sulfate with a mass fraction of 10% by an unsaturated impregnation method. Dry for 10 hours, then bake at 900°C for 4 hours. The unsaturated carrier after roasting is sprayed and dipped in morphine aqueous solution. The spray volume of morphine aqueous solution is 10% of the total saturated water absorption of the carrier used. The mass content of morphine in the morphine aqueous ...
example 3
[0030] Except that 5% ammonium citrate was added to the impregnated ferric nitrate aqueous solution, the rest was the same as in Example 1, and the prepared catalyst was denoted as C-3, and the 300h evaluation results were shown in Table 1.
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