Preparation method of catalyst for producing propylene by propane dehydrogenation under carbon dioxide atmosphere
A technology for dehydrogenation of carbon dioxide and propane, used in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, dehydrogenation to hydrocarbons, etc. In order to achieve the effect of low cost, good stability and high propylene yield
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Embodiment 1
[0021] Zn(NO 3 ) 2 Dissolve in water to prepare solution, Zn 2+ The ion concentration is 0.002g / mL, and the HZSM-5 zeolite with a silicon to aluminum ratio of 150 is added to the above Zn(NO 3 ) 2 In the solution, mix evenly to form a suspension. The liquid-to-solid ratio is 21.14mL / g when added. The suspension is heated and stirred under an infrared lamp to evaporate to dryness, dried at 90°C for 18 hours, and baked at 600°C for 7 hours in an air atmosphere , To obtain catalyst-1, wherein the active component zinc oxide loading is 5wt%. The reaction activity of propane dehydrogenation under a carbon dioxide atmosphere was measured on a continuous micro-reactor. The specific reaction conditions are as follows: the amount of catalyst is 0.2g, the reaction pressure is 1atm, the total flow of reactant gas is 20mL / min, of which the flow of propane is 0.5mL / min, the flow of carbon dioxide is 1mL / min, and the rest is high-purity nitrogen. Activate at 600°C for 2 hours, and the reacti...
Embodiment 2
[0023] Use the method of Example 1 to determine the CO content of Catalyst-1 2 The stability of the propane dehydrogenation reaction under the atmosphere, after 30 hours of reaction, the propylene yield was 25.8%, and the propylene selectivity was 62.1%.
Embodiment 3
[0025] ZnCl 2 Dissolve in water to prepare solution, Zn 2+ The ion concentration is 0.002g / mL, and the HZSM-5 zeolite with a silicon to aluminum ratio of 100 is added to the above ZnCl 2 In the solution, mix uniformly to form a suspension. The liquid-to-solid ratio is 21.14mL / g when added. The suspension is heated and stirred under an infrared lamp to evaporate to dryness, dried at 110°C for 24 hours, and baked at 650°C for 4 hours in an air atmosphere , To obtain catalyst-2, wherein the active component zinc oxide loading is 5wt%. Use the method of Example 1 to determine its CO 2 Propane dehydrogenation activity in atmosphere. In the steady state, the propylene yield on Catalyst-2 was 23.2%, and the propylene selectivity was 40.3%.
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