Catalyst used for acetylene method vinyl acetate synthesis
A vinyl acetate and catalyst technology, applied in the field of vinyl acetate synthesis, can solve problems such as low catalyst activity, and achieve the effect of improving catalyst activity
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Embodiment 1
[0018] (1) Catalyst preparation
[0019] (a) Preparation of impregnation solution: 0.45 g diethylene glycol dimethyl ether, 0.45 g dimethyl phthalate and 18.0 g Zn(OAc) 2 Dissolve in a mixed solvent of methanol and water (90 wt% methanol, 10 wt% water) at 50°C to prepare 180 ml of impregnation solution, in which Zn(OAc) 2 The content is 100 g / L, and the total content of diether and aromatic ester is 5.0 g / L;
[0020] (a) Impregnation of the carrier: the selected activated carbon is coal-based cylindrical carbon (2.4 mm in diameter, 2 cm in length), with a specific surface area of 1200 cm 2 / g, the total adsorption pore volume is 0.7 cm 3 / g; add 100 ml of the activated carbon carrier to the above impregnation solution, impregnate at 70°C for 4 h, and filter;
[0021] (b) Drying: Dry the catalyst at 105°C for 6 h. The catalyst can be evaluated for catalyst performance after being loaded into the reactor.
[0022] (2) Characterization of physical properties
[0023]The Zn...
Embodiment 2】 to 【 Embodiment 5
[0034] Except for changing the types of cocatalyst diether and 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 6
[0036] (1) Catalyst preparation
[0037] (a) Preparation of impregnation solution: 0.75 g diethylene glycol dimethyl ether, 0.15 g diethyl phthalate and 18.0 g Zn(OAc) 2 Dissolve in a mixed solvent of methanol and water (90 wt% methanol, 10 wt% water) at 50°C to prepare 180 ml of impregnation solution, in which Zn(OAc) 2 The content is 100 g / L, and the total content of diether and aromatic ester is 5.0 g / L;
[0038] (b) Impregnation of the carrier: the selected activated carbon is coal-based cylindrical carbon (diameter 2.4 mm, length 2 cm, specific surface area 1200 cm 2 / g, the total adsorption pore volume is 0.7 cm 3 / g; add 100 ml of the activated carbon carrier to the above impregnation solution, impregnate at 70°C for 4 h, and filter;
[0039] (c) Drying: Dry the catalyst at 105°C for 6 h, and the catalyst can be evaluated for catalyst performance after being loaded into the reactor.
[0040] The catalyst physical property characterization is the same as in Example 1...
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