A catalyst for directly producing low-carbon olefins from synthesis gas and its preparation and application
A low-carbon olefin and catalyst technology, applied in the field of iron-based catalysts, can solve the problems of complex catalyst composition, low CO conversion rate, complicated preparation process, etc., and achieve the effects of reducing selectivity, avoiding secondary reactions, and simple preparation method
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Embodiment 1
[0029] Take 1.523g of silicon carbide dried at 120°C for 10h, add 25mL of ferric nitrate solution containing 0.689g into the silicon carbide, stir continuously at room temperature for 10h, and then evaporate to dryness under negative pressure at 90°C, and dry at 120°C 12h, and then roasted in a muffle furnace at 350°C for 5h to obtain Fe 2 o 3 Catalyst A at 13% by weight.
Embodiment 2
[0031]Take 8.245g of manganese dioxide dried at 120°C for 10h, add 100mL of a solution containing 6.256g of ferric nitrate and 1.198g of ammonium molybdate into the manganese dioxide, stir continuously at room temperature for 10h, and then rotary evaporate at 90°C under negative pressure to Dry and dry at 120°C for 12h, and then bake in a muffle furnace at 450°C for 5h to obtain Fe 2 o 3 Content is 18.22wt%, MoO 3 Catalyst B at 9.01% by weight.
Embodiment 3
[0033] Take 4.526g of titanium dioxide dried at 120°C for 10h, add 50mL solution containing 4.256g of ferric nitrate and 0.322g of potassium nitrate into the titanium dioxide, stir continuously at room temperature for 10h, and then evaporate to dryness under negative pressure at 90°C and dry at 120°C Drying for 12 hours under the hood, and finally roasting in a muffle furnace at 450°C for 5 hours to obtain Fe 2 o 3 The content is 23.1wt%, K 2 Catalyst C with an O content of 5.3 wt%.
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