Process for preparing catalyst for preparing propylene with propane dehydrogenation in carbonic anhydride condition and uses thereof
A technology for dehydrogenation of carbon dioxide and propane, used in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of high price, poor stability, limitations, etc., and achieve low cost, good stability, and deactivation. slow effect
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example 1
[0021] Example 1: Zn(NO 3 ) 2 Soluble in water to make solution, Zn 2+ The concentration is 0.0021g / mL, and the HZSM-5 zeolite with a silicon-alumina ratio of 25 is treated with steam at 650°C for 6 hours, and then added to the above-mentioned Zn(NO 3 ) 2 In the solution, mix evenly to form a suspension, the liquid-solid ratio is 20mL / g when adding, heat and stir the suspension under an infrared lamp, evaporate to dryness, dry at 100°C for 24 hours, and roast at 600°C in an air atmosphere for 6 hours, Catalyst-1 was obtained, wherein the loading amount of the active component zinc oxide was 5 wt%. The reactivity of propane dehydrogenation under carbon dioxide atmosphere was determined in a continuous microreactor. The specific reaction conditions are as follows: the amount of catalyst is 0.2g, the reaction pressure is 1atm, the total flow rate of reaction gas is 20mL / min, wherein the flow rate of propane is 0.5mL / min, the flow rate of carbon dioxide is 1mL / min, and the res...
example 2
[0022] Example 2: Utilize the method of example 1 to measure catalyst-1 in CO 2 The stability of the propane dehydrogenation reaction under the atmosphere, after 30 hours of reaction, the yield of propylene was 20.3%, and the selectivity of propylene was 65.6%.
example 3
[0023] Example 3: Zn(CH 3 COO) 2 Soluble in water to make solution, Zn 2+ The concentration is 0.0014g / mL, the HZSM-5 zeolite with a silicon aluminum ratio of 25 is treated with steam at 600°C for 5 hours, and then added to the above Zn(CH 3 COO) 2 In the solution, mix evenly to form a suspension. When adding, the liquid-solid ratio is 30mL / g. The suspension is heated and stirred under an infrared lamp, evaporated to dryness, dried at 110°C for 12 hours, and roasted at 600°C in an air atmosphere for 8 hours. Catalyst-2 was obtained, wherein the loading amount of the active component zinc oxide was 5 wt%. Utilize the method of example 1 to measure its CO 2 Propane dehydrogenation activity under atmosphere. At steady state, the propylene yield on Catalyst-2 was 21.4%, and the propylene selectivity was 74.1%.
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