Compound catalyst and method for preparing styrene
A catalyst and styrene technology, applied in chemical instruments and methods, organic compound/hydride/coordination complex catalysts, physical/chemical process catalysts, etc., can solve the loss of catalysts and styrene, the intensification of side reactions of heavy components, High reaction temperature and other problems, to achieve the effect of increased device operation flexibility, reduced residence time, and small reactor volume
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Embodiment 1~11
[0056] Control the pressure of the flash tank at 50kPa, the pressure at the top of the separation tower at 30kPa, the temperature of the dehydration reactor at 200°C and the pressure at 50kPa, based on the weight of the freshly added 1-phenylethanol feedstock, the ratio of methanesulfonic acid and p-phenolic acid The compound catalyst is added according to the compound ratio n, and the circulation ratio (the weight of the heavy component of the circulating circulating reaction medium to the feed mass ratio of the freshly added 1-phenylethanol) is 10:1 to 32:1. The obtained styrene-containing material is adsorbed and deacidified by D301 alkaline resin, and the space velocity of the resin adsorption bed is 0.5BV. The results are shown in Table 1 below.
[0057] Table 1
[0058]
[0059]
Embodiment 12~18
[0061] The circulation ratio is 15 and the residence time is 60s. Based on the weight of the freshly added 1-phenylethanol raw material, the methanesulfonic acid and p-phenolic acid catalysts are compounded in a ratio of 1:1, the compounded catalyst is added at 100 ppm, and the flash tank pressure is P 1 kPa, separation tower top pressure P 2 kPa, where the pressure of the dehydration reactor is the same as the pressure of the flash tank, which is P 1 kPa. The obtained styrene-containing material is adsorbed and deacidified by D301 alkaline resin, and the space velocity of the resin adsorption bed is 0.5BV. The results of the reaction are shown in Table 2.
[0062] Table 2
[0063]
[0064]
[0065] The results show that by controlling the temperature of the dehydration reactor R-1 and adjusting the circulation ratio, the conversion rate of 1-phenylethanol can reach more than 98%, and the selectivity can reach more than 98.5%.
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