Ruthenium supported perovskite-type-oxide ammonia synthesis catalyst and preparation method thereof
A composite oxide and perovskite-type technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, preparation/separation of ammonia, etc., can solve low-temperature and low-pressure activity of ruthenium catalysts, etc. problems, achieve excellent catalytic activity, no loss of raw materials, and simple preparation process
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Embodiment 1
[0019] Zr(NO 3 ) 4 .5H 2 O:Ba(NO 3 ) 2 : A mixture of citric acid with a molar ratio of 1:1:2.0 was dissolved in a small amount of distilled water to obtain a colorless clear viscous liquid. The solution was slowly heated in a water bath at 80°C for 4 h to evaporate excess water, and then heated at a constant temperature of 90°C for 12 h to promote the gelation of the mixture. Finally, the obtained yellow gel was calcined at 300 °C for 1 h to obtain the precursor, and then calcined at 700 °C for 5 h to obtain BaZrO 3 carrier material. The active component ruthenium was impregnated into the carrier by equal volume impregnation method, and then reduced with absolute ethanol. The active component Ru accounted for 4% of the mass fraction of the carrier. The catalyst is 3 MPa, the space velocity is 10000 h -1 At 375°C, 400°C and 425°C, the outlet ammonia concentrations were 3.94%, 6.80% and 8.33%, respectively. Ammonia synthesis catalyst Ru / Al with 5wt% ruthenium content re...
Embodiment 2
[0021] BaZrO 3 The loading method of carrier and ruthenium is the same as embodiment 1, but the precursor of Zr is ZrO(NO 3 ) 2 . The outlet ammonia concentrations of the tested catalysts under the same conditions were 3.84%, 6.56% and 8.24%, respectively.
Embodiment 3
[0023] BaZrO 3 The loading method of carrier and ruthenium is the same as embodiment 1, but the precursor of Ba in the preparation process is Ba(CH 3 COO) 2 . The outlet ammonia concentrations of the tested catalysts under the same conditions were 3.72%, 5.94% and 7.86%, respectively.
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