Catalyst for synthesizing vinyl acetate by ethylene method and preparation method thereof
A vinyl acetate and catalyst technology, applied in the field of ethylene gas phase vinyl acetate catalyst, can solve the problems of low space-time yield and selectivity of the catalyst, and achieve the effects of increased selectivity, enhanced selectivity, and good technical effects
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Embodiment 1
[0029] (1) Catalyst preparation
[0030] (a) Take H 2 PdCl 4 and HAuCl 4 1000ml of the aqueous solution is the impregnation solution (palladium content: 2.75g / L, gold content: 0.625g / L), impregnating 1100ml of spherical silica carrier with a diameter of 5.8mm (BET specific surface 175cm 2 / g, the pore volume is 0.7cm 3 / g) 3hr to obtain catalyst precursor I;
[0031] (b) 27.5gNa 2 SiO 3 9H 2 O was made into 100ml aqueous solution and added to the above-mentioned catalyst precursor I, shaken several times to avoid agglomeration, allowed to stand for 24 hours, and then dried at 80°C for 8 hours to obtain catalyst precursor II;
[0032] (c) Catalyst precursor II was reduced in a hydrogen atmosphere (flow rate of 0.2ml / min, temperature of 150°C) for 2 hours and then lowered to room temperature to obtain catalyst precursor III;
[0033] (d) Take 450ml of a mixed solution of methanol and water containing KOAc and methyl benzoate (the weight percentage of methanol and water is ...
Embodiment 2
[0047] [Example 2] to [Example 6]
[0048] Except for changing the type of co-catalyst aromatic acid ester in the catalyst preparation process, other operating steps and evaluation conditions were the same as in Example 1. For the convenience of comparison, the catalyst preparation conditions are listed in Table 1, and the catalyst evaluation conditions and characterization evaluation results are listed in Table 2.
Embodiment 7
[0050] (1) Catalyst preparation
[0051] (a) Take H 2 PdCl 4 and HAuCl 4 1000ml of the aqueous solution is the impregnation solution (palladium content: 2.75g / L, gold content: 0.625g / L), impregnating 1100ml of spherical silica carrier with a diameter of 5.8mm (BET specific surface 175cm 2 / g, the pore volume is 0.7cm 3 / g) 3hr to obtain catalyst precursor I;
[0052] (b) 27.5gNa 2 SiO 3 9H 2 O was made into 100ml aqueous solution and added to the above-mentioned catalyst precursor I, shaken several times to avoid agglomeration, allowed to stand for 24 hours, and then dried at 80°C for 8 hours to obtain catalyst precursor II;
[0053] (c) Catalyst precursor II was reduced in a hydrogen atmosphere (flow rate of 0.2ml / min, temperature of 150°C) for 2 hours and then lowered to room temperature to obtain catalyst precursor III;
[0054] (d) Take 450ml of a mixed solution of methanol and water containing KOAc, methyl benzoate and dimethyl phthalate (the weight percentage of ...
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