Preparation method of super-crosslinked polymer supported molecular sieve and Fe catalyst and application of super-crosslinked polymer supported molecular sieve and Fe catalyst in production of divinylbenzene
A technology of loading molecules and divinylbenzene, applied in molecular sieve catalysts, including molecular sieve catalysts, carbon compound catalysts, etc., can solve the problems of mismatch between catalytic performance and production demand, product quality, long catalyst induction period, and reduced catalytic efficiency. Excellent pore shape selection function, avoiding high consumption and improving catalytic activity
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Embodiment 1
[0027] The preparation method of hypercrosslinked polymer-loaded ZSM-5 molecular sieve and Fe catalyst is: in a 50ml two-neck round bottom flask, add 0.9302g of bis-ferrocene, 0.39g of benzene and 0.4948g of 1,2-dichloro Ethane, then add the external crosslinking agent dimethoxymethane FDA, set up a condensing reflux device, continue to stir for 30min, then quickly add 0.8110g anhydrous FeCl3 to the above device to obtain the mixture K, and then heat the mixture K from room temperature React at 45°C for 5h, continue to heat up to 80°C for 19h, and complete the condensation polymerization reaction to form a microporous structure. After the reaction, the product is centrifugally washed with methanol, and vacuum-dried at 60°C for 24h to obtain an iron-based hypercrosslinked polymer. Dissolve the obtained iron-based hypercrosslinked polymer, add 1g of ZSM-5 molecular sieve, stir for 4h, let it stand for 12h, centrifuge dry for 12h, and roast at 500°C for 5h, finally get the hypercr...
Embodiment 2
[0031] Same as Example 1, the reaction temperature is set to 250°C, the space velocity is changed, and the reaction results are shown in Table 2,
[0032] Table 2
[0033] Volumetric space velocity / h -1
Embodiment 3-6
[0035] Same as Example 2, the reaction temperature is set to 250°C, the reaction pressure is changed, and the reaction results are shown in Table 3,
[0036] table 3
[0037] Reaction pressure / MPa Ethylbenzene conversion / % Divinylbenzene selectivity / % Divinyl benzene yield / % 0.1 75.12 90.39 67.90 0.3 74.47 90.28 67.23 0.4 75.39 91.56 69.03 0.5 76.92 90.98 69.98
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