Catalyst for producing vinyl acetate by acetylene method and preparation method and use thereof
A vinyl acetate and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, etc., can solve the problems of low production capacity, high reaction temperature and high cost , to achieve the effect of good catalytic performance, good mechanical strength and easy loading
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[0012] Example 1:
[0013] Acrylonitrile and vinylidene chloride were distilled to remove the polymerization inhibitor to obtain monomers, and the molar ratio of acrylonitrile and vinylidene chloride was 1.5:10. The initiator is azobisisoheptonitrile, and the amount is 1-2% (molar ratio) of the monomer amount. The copolymer pellets are obtained by suspension polymerization. The particle size of the polymer pellets is controlled by adjusting the stirring speed. The polymerization temperature is 40℃, polymerization time is 24 hours. After the reaction, the pellets are repeatedly washed with boiling water to remove the dispersant. The polymer pellets are put into a quartz tube, and the temperature is gradually raised to 1000℃ under the protection of argon and kept at 1 -3 hours to obtain the copolymer-derived carbon pellet catalyst carrier. The above method is used to obtain carbon pellet carriers with different ratios of acrylonitrile and vinylidene chloride.
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[0014] Example 2:
[0015] Weigh 30 g of the derivatized carbon prepared in Example 1, and calculate the amount of mixed solution required for impregnation. Weigh 1.92g Zn(CH 3 COO) 2 ·2H 2 O was dissolved in a mixed solvent of methanol and water, zinc acetate was loaded on the derivatized carbon by an equal volume impregnation method, and after drying, a catalyst for the production of vinyl acetate with a zinc acetate loading of 5% was obtained.
[0016] Using the above method, catalysts with different zinc acetate loadings were prepared.
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[0017] Example 3
[0018] 20g of catalysts with different loadings of zinc acetate were loaded into the fixed bed reactor. The heating medium of the reactor is heat-conducting silicone oil. Acetylene comes from a steel cylinder, and acetic acid is pumped in by a metering pump. The reaction products are collected in the condenser and analyzed quantitatively by chromatography. By changing the reaction temperature and the space velocity of the gas, the reaction results under different reaction conditions are obtained, as shown in Table 1.
[0019] Table 1 Catalytic reaction results of the catalyst with a zinc acetate loading of 5wt%
[0020]
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