Method for catalytically synthesizing paraethyl phenol
A technology for ethyl phenol and phenol, applied in the field of catalytic synthesis of p-ethyl phenol, can solve the problems of affecting catalyst stability, low product quality, low stability, etc., and achieves convenient product separation, high raw material activity, and warm reaction conditions. Effect
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Embodiment 1
[0023] Using modified ZSM-5 as a catalyst, wherein the concentration of cetylpyridine bromide solution used in the modification process is 200mmol / L, the loading capacity of phosphoric acid is 2.5%, with diethyl carbonate and phenol as raw materials, at the reaction temperature The temperature is 320°C, the molar ratio of raw materials diethyl carbonate and phenol is 1:1, and the mass space velocity is 10h -1 under the conditions. The conversion rate of phenol reaches 46.7%, and the selectivity to p-ethylphenol is 65.8%.
Embodiment 2
[0025] Using modified ZSM-5 as a catalyst, wherein the concentration of cetylpyridinium bromide solution used in the modification process is 100mmol / L, the phosphoric acid loading is 2.5%, with diethyl carbonate and phenol as raw materials, at the reaction temperature The temperature is 320°C, the molar ratio of raw materials diethyl carbonate and phenol is 1:1, and the mass space velocity is 10h -1 under the conditions. The conversion rate of phenol reaches 47.2%, and the selectivity to p-ethylphenol is 59.3%.
Embodiment 3
[0027] Using modified ZSM-5 as a catalyst, wherein the concentration of cetylpyridine bromide solution used in the modification process is 400mmol / L, the phosphoric acid loading is 2.5%, with diethyl carbonate and phenol as raw materials, at the reaction temperature The temperature is 320°C, the molar ratio of raw materials diethyl carbonate and phenol is 1:1, and the mass space velocity is 10h -1 under the conditions. The conversion rate of phenol reaches 45.1%, and the selectivity to p-ethylphenol is 66.1%.
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