A kind of methyl acrylate hydrogenation methyl propionate catalyst and its preparation and application
A technology for preparing methyl acrylate and methyl propionate, which is applied in catalyst activation/preparation, carboxylate preparation, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of low selectivity of methyl propionate, High reaction temperature, difficult separation and other problems, to achieve the effect of good dispersion, low reaction temperature and low pressure
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Embodiment 1
[0025] The preparation process of the present embodiment methyl acrylate hydrogenation methyl propionate catalyst is as follows:
[0026] 1. Mix cerium nitrate and benzyl alcohol according to the molar ratio of 1:4, heat and reflux at 90°C for 2 hours after mixing evenly, and continue to reflux after water removal treatment (after about 1 hour of reflux process, open for about 10 minutes). 3h, centrifuged and washed 3 times, dried at 100°C for 4h, and calcined at 350°C for 4h to obtain a cerium oxide carrier;
[0027] 2. Take a certain amount of RuCl 3 ·3H 2 O, Ni(NO 3 ) 2 , Cu(NO 3 ) 2 Prepare an aqueous solution, Ru: (Cu+Ni) molar ratio=1:0.4, Cu:Ni molar ratio=1:2, the mixed solution of Ru, Cu and the cerium oxide carrier after roasting in step 1 carry out equal-volume impregnation for 4h, After impregnation, it was dried at 90°C for 4h and calcined at 400°C for 12h; the Ru loading was 0.4% by mass.
[0028] In the catalyst of this embodiment, the percentage content ...
Embodiment 2
[0030] The preparation process of the present embodiment methyl acrylate hydrogenation methyl propionate catalyst is as follows:
[0031] 1. Mix cerium nitrate and benzyl alcohol according to the molar ratio of 1:6. After mixing evenly, heat and reflux at 100°C for 4h. After dehydration treatment, continue to reflux for 5h, centrifuge and wash 3 times, dry at 110°C for 6h, and roast at 300°C. After 12h, the cerium oxide carrier was obtained;
[0032] 2. Take a certain amount of Pd(NO 3 ) 2 , Ni(NO 3 ) 2 Prepare an aqueous solution with a molar ratio of Pd:Ni=1:0.3, impregnate the mixed solution of Pd and Ni with the cerium oxide support calcined in step 1, dry at 90°C for 12h, and calcinate at 450°C for 12h; wherein the Pd load is mass Percentage 0.3%.
[0033] In the catalyst of this example, the percentage content of active component Pd is 0.3%, the percentage content of Ni is 0.05%, and the rest is carrier. The resulting catalyst is designated as D2.
Embodiment 3
[0035] The preparation process of the present embodiment methyl acrylate hydrogenation methyl propionate catalyst is as follows:
[0036] 1. Mix cerium nitrate and benzyl alcohol according to the molar ratio of 1:8. After mixing evenly, heat and reflux at 90°C for 3h. After dehydration treatment, continue to reflux for 8h, centrifuge and wash 3 times, dry at 120°C for 20h, and roast at 350°C. After 8h, the cerium oxide carrier was obtained;
[0037] 2. Take a certain amount of H 2 PtCl 6 ·6H 2 O, Cu(NO 3 ) 2 Prepare an aqueous solution with a molar ratio of Pt:Cu=1:0.2, impregnate the mixed solution of Pt and Ni with the calcined cerium oxide support in step 1, dry at 100°C for 24h, and calcinate at 350°C for 8h; wherein the Pt load is the mass Percentage 0.6%.
[0038] In the catalyst of this example, the percentage content of active component Pt is 0.6%, the percentage content of Cu is 0.04%, and the rest is carrier. The resulting catalyst is designated D3.
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