Method for producing propylene by disproportionation of butene and ethylene
A technology of ethylene and butene, applied in chemical instruments and methods, catalyst activation/preparation, catalysts, etc., can solve the problems of poor catalyst stability and achieve the effect of enhanced stability and increased specific surface area
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Embodiment 1
[0029] Weighed 1g of lithium hydroxide to make a solution, weighed 20g of magnesium oxide and mixed it, stirred at 70°C for 10h, dried the product obtained after suction filtration at 70°C for 10h, and then calcined at 500°C for 6h. The obtained product was designated as JT-1. The specific surface area and surface basic site concentration of oxides are shown in Table 1.
Embodiment 2
[0031] Weigh 5g of sodium carbonate to make a solution, weigh 20g of magnesium oxide and mix it, add 0.1g of auxiliary copper oxide, stir at 40°C for 15h, and dry the product obtained after suction filtration at 40°C for 16h, then mix with 3g of activated carbon Mix and impregnate, dry and bake at 800°C for 3h. The obtained product was designated as JT-2. The specific surface area and surface basic site concentration of oxides are shown in Table 1.
Embodiment 3
[0033] Weigh 8g of potassium nitrate to make a solution, weigh 20g of calcium oxide and mix it, add 0.8g of additive zinc oxide, stir at 120°C for 5h, and dry the product obtained after suction filtration at 100°C for 6h, then mix with 2g of SiO 2Mix and impregnate, dry and bake at 350°C for 10h. The resulting catalyst product is designated as JT-3. The specific surface area and surface basic site concentration of oxides are shown in Table 1.
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Abstract
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