Green and efficient heterogeneous catalyst for compounding 2,4-di-tert-butylphenol
A di-tert-butylphenol and heterogeneous catalyst technology, applied in the chemical industry, can solve the problems of high corrosion, easy pollution, high reaction temperature, etc., and achieve the effects of reducing operating costs, simplifying the production process, and stabilizing catalytic performance
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Embodiment 1
[0017] 40wt% styrene monomer, 7wt% dipropenylbenzene copolymerized crosslinking monomer, 3wt% azobisisobutyronitrile initiator, 8wt% acetone esterified modified nano-CaCO 3 Materials, 12wt% toluene porogen and 30wt% petroleum ether solvent are formulated into oil phase solution A; pure water, Arabic dispersant and iron oxide dispersant are formulated into water phase solution B at a mass ratio of 100:2:1.8. Then the oil phase solution A and the water phase solution B were mixed according to the mass ratio of 1:2.4, vigorously stirred at 80°C for 6 hours, filtered and washed to obtain polymer microspheres containing modified porous nanomaterials; then steam distillation was used The porogen and residual monomers were removed at 95°C, and the obtained porous resin bulk white ball was stirred in 2% hydrochloric acid at 50°C for 5 h, washed with water, filtered, and dried to obtain the bulk resin microspheres containing nanopores. ball.
[0018] According to the mass ratio of 100...
Embodiment 2
[0020] After preheating at 78°C, 2000 kg of phenol was fed into the tank reactor in the form of fluid, and 30 kg of the solid acid resin catalyst obtained in Example 1 was added, and stirred for 20 min. 1790 kg of isobutylene was introduced at a rate of 800 kg / h, and the temperature of the reaction system was set at 95°C. When the temperature was higher than 95°C, high-speed circulating cooling water was used to cool down. After the isobutene was completely introduced, the reaction system was kept warm for 60 min. After the reaction was completed, the catalyst was kept in the reactor, and then the 2,4-di-tert-butylphenol was alkylated and squeezed out, and the content of 2,4-di-tert-butylphenol was analyzed to be 70.65%.
Embodiment 3
[0022] After preheating at 78°C, 3000 kg of phenol was fed into the tank reactor in the form of fluid, and 45 kg of the solid acid resin catalyst obtained in Example 1 was added, and stirred for 20 min. 3040 kg of isobutylene was introduced at a rate of 800 kg / h, and the temperature of the reaction system was set at 97°C. When the temperature was higher than 97°C, high-speed circulating cooling water was used to cool down. After isobutene was completely introduced, the reaction system was kept warm for 30 min. After the reaction was completed, the catalyst was kept in the reactor, and then the 2,4-di-tert-butylphenol was alkylated and squeezed out, and the content of 2,4-di-tert-butylphenol was analyzed to be 72.58%.
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