Catalyst for improving methanol aromatization reaction performance, and preparation method and application thereof
A reaction performance, catalyst technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of reducing catalyst wear resistance, tedious HZSM-5, low selectivity of aromatics, etc., to achieve improved Anti-carbon performance, low price, and the effect of improving the selectivity of aromatics
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Embodiment 1
[0036] Take 0.55g of nitric acid and 1.88g of ferric nitrate in a 25ml beaker, add 2.5g of deionized water, seal and ultrasonically disperse the solution for 20min; Ferric nitrate and gallium nitrate solutions are evenly impregnated in the zeolite channels, then dried in a blast drying oven at 80°C, placed in an air atmosphere, and baked at 550°C in a muffle furnace at a heating rate of 2°C / min After 6 hours, a finished catalyst with a loading capacity of 3%Ga5%Fe / HZSM-5 was obtained.
[0037] A continuous-flow fixed-bed reactor was used to evaluate the effect of the methanol aromatization catalyst. The reactor was a U-shaped steel pipe with an inner diameter of 8 mm; the catalyst was filled, and the upper layer of the catalyst was covered with quartz wool to ensure that the bed was evenly distributed. Before the reaction, the catalyst was heated in H 2 In situ reduction at a flow rate of 25mL / min and a temperature of 500°C for 1h, then cooled to a reaction temperature of 400°...
Embodiment 2
[0041]Take 0.367g of nitric acid and 2.16g of ferric nitrate in a 25ml beaker, add 2.5g of deionized water, seal and ultrasonically disperse the solution for 30min; Ferric nitrate and gallium nitrate solutions are evenly impregnated in the zeolite channels, then dried in a blast drying oven at 80°C, placed in a nitrogen atmosphere, and baked at 500°C in a muffle furnace at a heating rate of 5°C / min After 6 hours, a finished catalyst with a loading capacity of 2%Ga-7%Fe / HZSM-5 was obtained.
[0042] A continuous-flow fixed-bed reactor was used to evaluate the effect of the methanol aromatization catalyst. The reactor was a U-shaped steel pipe with an inner diameter of 8 mm; the catalyst was filled, and the upper layer of the catalyst was covered with quartz wool to ensure that the bed was evenly distributed. Before the reaction, the catalyst was heated in H 2 In situ reduction at a flow rate of 25mL / min and a temperature of 500°C for 1h, then cooled to a reaction temperature of...
Embodiment 3
[0044] Take 0.13g of nitric acid and 0.43g of ferric nitrate in a 25ml beaker, add 2.5g of deionized water, seal and ultrasonically disperse the solution for 60min; Ferric nitrate and gallium nitrate solutions are evenly impregnated in the zeolite channels, then dried in a blast oven at 80°C, placed in an air atmosphere, and baked in a muffle furnace at a heating rate of 3°C / min to 600°C After 6 hours, a finished catalyst with a loading capacity of 1%Ga-1%Fe / HZSM-5 was obtained.
[0045] A continuous-flow fixed-bed reactor was used to evaluate the effect of the methanol aromatization catalyst. The reactor was a U-shaped steel pipe with an inner diameter of 8 mm; the catalyst was filled, and the upper layer of the catalyst was covered with quartz wool to ensure that the bed was evenly distributed. Before the reaction, the catalyst was heated in H 2 In situ reduction at a flow rate of 25mL / min and a temperature of 500°C for 1h, then cooled to a reaction temperature of 400°C, and...
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