Rare-earth oxide modified high-selectivity catalyst for adiponitrile hydrogenation and hexylenediamine production, preparation method and application thereof
A rare earth metal, high-selectivity technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, preparation of organic compounds, preparation of amino compounds, etc. High mechanical strength, reduced environmental pollution, mild reaction conditions
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Embodiment 1
[0030] Prepare a certain concentration of nickel nitrate, aluminum nitrate and cerium nitrate metal salt precursors, and mix them uniformly by ultrasonic to form a mixed solution A. Sodium carbonate solution B with pH = 11 was prepared in deionized water. Under constant temperature and stirring conditions of 45°C, the above two clear solutions A and B were dripped into deionized water side by side, and the dropping speed was controlled to be 3 s / drop. Continue to adjust with sodium carbonate solution until pH=10. After aging for 8 hours, filter, wash, and dry at 110°C for 10 hours with deionized water and methanol, and roast the ground powder in a tube furnace at 400°C for 4 hours to obtain a catalyst precursor. Catalyst precursor in H 2 / Ar mixed gas at 400°C for 6 h to obtain catalyst powder. figure 1 Exhibit 2wt% CeO 2 X-ray diffraction (XRD) pattern of the modified nickel-based catalyst. figure 2 Exhibit 2wt% CeO 2 Modified Ni-based catalyst samples (2%) in NH 3 Te...
Embodiment 2
[0032] 2.5g of adiponitrile, 25ml of absolute ethanol and reduction pretreated 0.5g of CeO 2 The mass percentage is 2wt% Ni / CeO 2 / Al 2 o 3 Add the catalyst into a 50ml high-pressure closed reaction kettle, and replace the air in the kettle with hydrogen for 2-3 times. The stirring speed is 800rpm, and the reaction time is 3h. image 3 and Figure 4 Demonstration of 2wt% CeO after pretreatment 2 Modified Ni / CeO 2 / Al 2 o 3 Transmission electron micrograph of the catalyst. See Table 1 below for Ni / CeO under different reaction conditions 2 / Al 2 o 3 Test results for liquid-phase catalytic hydrogenation of adiponitrile.
[0033] Table 1 2wt% CeO at different reaction temperatures 2 Modified Ni / CeO 2 / Al 2 o 3 Test results of liquid-phase catalytic hydrogenation of adiponitrile
[0034]
Embodiment 3
[0036] 2.5g of adiponitrile, 25ml of absolute ethanol and reduction pretreated 0.5g of CeO 2 The mass percentage is 1wt% Ni / CeO 2 / Al 2 o 3 Catalyst The catalyst is added to a 50ml high-pressure reaction kettle, and the air in the kettle is replaced with hydrogen for 2-3 times. The stirring speed is 800 rpm, the reaction time is 3 h, the reaction temperature is 90° C., the hydrogen pressure is 7 MPa, the conversion rate of adiponitrile is 100%, and the selectivity of hexamethylenediamine is 70%. High-purity hexamethylenediamine can be obtained after distillation and purification under reduced pressure.
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