Vinyl acetate preparation method
A vinyl acetate and ethylene technology, applied in the field of vinyl acetate preparation, can solve the problems of low space-time yield and selectivity, and achieve the effects of improving space-time yield and selectivity, good technical effect, and improved selectivity
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Embodiment 1
[0010] (1) Catalyst preparation
[0011] Step (a): Take 1200ml of liquid carbon dioxide solution containing hexafluoroacetylacetonate palladium (II) and dimethyl (trifluoroacetylacetonate) gold (III) as the impregnating liquid, the palladium content of this impregnating liquid is 2.75g / L, gold content of 0.625g / L, impregnating 1100ml of a spherical silica carrier with a diameter of 4-6mm at an impregnation pressure of 69MPa and an impregnation temperature of 28°C to obtain catalyst precursor I;
[0012] Step (b): Then reduce the pressure and evaporate the liquid carbon dioxide in the catalyst precursor I at a rate of 0.3ml (liquid carbon dioxide) / min until the liquid carbon dioxide evaporates completely to obtain the catalyst precursor II;
[0013] Step (c): reducing the catalyst precursor II in a hydrogen atmosphere, the hydrogen flow rate is 0.2ml / min, and the reduction temperature is 75°C to obtain the catalyst precursor III;
[0014] Step (d): soak the catalyst precursor ...
Embodiment 2
[0029] Except that the roasting step is added between step (c) and step (d), other steps are all the same as in Example 1. Wherein the roasting step is: the catalyst precursor III is roasted under a nitrogen / acetic acid atmosphere, wherein the partial pressure of acetic acid accounts for 5% of the total pressure, the roasting temperature is 250°C, and the roasting time is 24hr. For the convenience of comparison, the preparation conditions of the catalyst are listed in Table 1, the physical property data of the catalyst are listed in Table 2, and the evaluation conditions, space-time yield and selectivity data of the catalyst are listed in Table 3.
Embodiment 3~14
[0031] In addition to changing the concentration of palladium in the liquid carbon dioxide impregnating solution, the type of palladium-gold compound, the concentration of potassium acetate solution, impregnating pressure, impregnating temperature, reducing gas, reducing temperature, molar ratio of reaction raw materials, space velocity of raw material gas, reaction pressure and reaction Except temperature, other operation steps are all identical with embodiment 2. For the convenience of comparison, the preparation conditions of the catalyst are listed in Table 1, the physical property data of the catalyst are listed in Table 2, and the evaluation conditions, space-time yield and selectivity data of the catalyst are listed in Table 3.
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