Catalyst for hydrodeoxygenation reaction of biodiesel, preparation method and applications thereof
A biodiesel and deoxygenation reaction technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, carbon compound catalyst, liquid hydrocarbon mixture preparation, etc., can solve the problem of low utilization rate and catalytic efficiency, carrier acid center residue, Low economy of H atoms and other problems, to achieve high metal utilization, improve dispersion, and improve product selectivity.
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Embodiment 1
[0037] Catalyst preparation
[0038] (1) Catalyst carrier preparation. Weigh 60.294g Al(NO 3 ) 3 9H 2 O (molecular weight: 375), 0.630g Mn (NO 3 ) 2 (molecular weight: 179) and 2.559g Ba(NO 3 ) 2 (Molecular weight: 261) was dissolved in 150ml of deionized water to form a solution, and stirred for 1h; the solution was heated to 60°C, neutralized with 5wt% sodium carbonate solution, and the pH was controlled to be 9; after filtering and washing with deionized water, use 10mol / L nitric acid solution acidified to pH 6, stirred until it was in the form of a sol, and the carrier slurry was obtained; the slurry was added dropwise to the oily ammonia column, and the sol shrank into a spherical gel, and after aging for 2 hours, the gel pellet was taken out and washed with deionized water , drying at 120°C for 12 hours, and calcining at 500°C for 8 hours to obtain composite oxide carrier pellets;
[0039] (2) Weigh 0.057g SnCl 2 2H 2 O (molecular weight: 226) and 0.120g H 2 ...
Embodiment 2
[0043] The catalyst preparation process is the same as in Example 1.
[0044] Catalyst evaluation: The evaluation conditions were the same as in Example 1, and the evaluation raw material was changed to methyl oleate. The specific conditions are that the reactor adopts a radial reactor, and the reaction temperature of hydrogenation bed I (filled with basic alumina, Shanghai Yuanjiang Chemical, 80-160 mesh) and hydrogenation bed II (filled with catalyst A) is 45°C, The reaction pressure is 4.0MPa, the molar ratio of hydrogen to methyl oleate (18:1) is 0.5, and the liquid hourly space velocity is 4h -1 . The catalyst needs to be reduced with pure hydrogen before the reaction, the reduction temperature is 500°C, and the reduction time is 3h. The catalyst of cracking bed III is ZSM-5 type catalytic material, the process conditions are 600°C and the space velocity is 10h -1 , the reaction pressure is 4.0MPa, and the catalyst-oil ratio is 8. The catalytic effect is shown in Table...
Embodiment 3
[0046] (1) Catalyst carrier preparation. Weigh 57.904g Al(NO 3 ) 3 9H2O (molecular weight: 375), 0.756g Mn(NO 3 ) 2 (Molecular weight: 179) and 3.071g Ba(NO 3 ) 2 (Molecular weight: 261) was dissolved in 150ml of deionized water to form a solution, and stirred for 1h; the solution was heated to 45°C, neutralized with 5wt% sodium carbonate solution, and the pH was controlled to be 9; after filtering and washing with deionized water, use 10mol / L nitric acid solution acidified to pH 6, stirred until it was in the form of a sol, and the carrier slurry was obtained; the slurry was added dropwise to the oily ammonia column, and the sol shrank into a spherical gel, and after aging for 2 hours, the gel pellet was taken out and washed with deionized water , drying at 160°C for 18 hours, and calcining at 550°C for 8 hours to obtain composite oxide carrier pellets;
[0047] (2) Weigh 0.028g SnCl 2 2H 2 O (molecular weight: 226) and 0.060g H 2 PtCl 6 ·6H 2 O (molecular weight:...
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