Catalyst for preparing acetone from acetic acid and its synthesis method and application
A catalyst, acetic acid technology, applied in chemical instruments and methods, organic chemistry, carbon-based compound preparation and other directions, can solve the problem of high cost, achieve the effect of low cost, small separation load, and easy industrial application
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Embodiment 1
[0026] Weigh 3.2gSiO2 2 , 6.8g of high-purity calcium aluminate cement (the manufacturer is "Kaifeng Hecheng Special Refractories Co., Ltd.", the specification model is high-purity CA-75, and the high-purity calcium aluminate adopted in the following examples without special instructions is this model ), after being pulverized and mixed, ball milled for 6 hours, the sample was formed by extrusion, and the obtained strip carrier was roasted at 300°C for 5 hours, and the mass fraction of the obtained composite was SiO 2 =32%, cement=68%.
[0027] Weigh 0.37gZr(NO 3 ) 4 ·5H 2 O, made into an aqueous solution, using the above-mentioned compound as a carrier, prepared by an equal volume impregnation method, dried at 100°C for 24h, and calcined at 350°C for 6h to obtain a catalyst composed of ZrO 2 =2.12%, carrier=97.88%. The obtained catalyst was loaded into the reactor, and the temperature was directly raised to 280°C, and the -1 Under the conditions, the conversion rate of ...
Embodiment 2
[0029] Weigh 5.8gSiO2 2 , 4.2g cement, crushed and mixed, ball milled for 10h, the sample was formed by pelleting, the obtained columnar carrier was roasted at 500°C for 3h, and the mass fraction of the obtained composite was SiO 2 =58%, cement=42%.
[0030] Weigh 1.6gLa(NO 3 ) 3 ·6H 2 O, made into an aqueous solution, using the above-mentioned compound as a carrier, prepared by an equal volume impregnation method, dried at 110°C for 15 hours, and calcined at 420°C for 5 hours to obtain a catalyst composed of La 2 o 3 =6.02%, carrier=93.98%. The obtained catalyst was loaded into the reactor, and the temperature was directly raised to 340°C, and the reaction pressure was 0.1MPa, and the mass space velocity was 2.0h. -1 Under the conditions, the conversion rate of acetic acid is 80.2%, and the selectivity of acetone is 99.1%.
Embodiment 3
[0032] Weigh 4.5gSiO 2, 5.5g of cement, crushed and mixed, ball milled for 8h, the sample was formed by pelletizing, the obtained columnar carrier was roasted at 400°C for 4h, and the mass fraction of the obtained composite was SiO 2 =45%, cement=55%.
[0033] Weigh 2.5gCe(NO 3 ) 3 ·6H 2 O, made into an aqueous solution, using the above-mentioned compound as a carrier, prepared by an equal volume impregnation method, dried at 120°C for 12 hours, and calcined at 500°C for 3 hours to obtain a catalyst composed of CeO 2 =9.91%, carrier=90.09%. The obtained catalyst was loaded into the reactor, and the temperature was directly raised to 400°C, and the -1 Under the conditions, the conversion rate of acetic acid is 85.2%, and the selectivity of acetone is 98.2%.
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Abstract
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