Refining method of styrene
A purification method, technology of styrene, applied in chemical instruments and methods, purification/separation of hydrocarbons, purification/separation of chemical modification, etc., can solve problems such as unfavorable environmental protection, low efficiency, toxicity and so on
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Embodiment 1
[0026] 1 Preparation of catalyst
[0027] Weigh according to mass ratio: 10% ferric oxide, 15% potassium chromate, 2.4% calcium oxide, 12% zinc oxide, 6.2% aluminum oxide, and mix evenly to obtain a finished catalyst.
[0028] 2 catalytic reaction
[0029] Add above-mentioned catalyst in the crude product of styrene that contains ethylbenzene, the ratio of its addition is 100mg / l; Control reaction temperature is 550 ℃, reaction system pressure 0.7 atmospheric pressure, pass into reaction polymerization inhibitor in reaction system simultaneously, with To avoid self-polymerization of styrene monomers, the polymerization inhibitor is hydrogen peroxide vapor, and the amount of hydrogen peroxide vapor introduced is 2 / 3 of the volume of the reaction vessel.
[0030] (c) Sampling and testing the content of ethylbenzene in the styrene product obtained from the reaction. When the content of ethylbenzene is less than 0.1%, stop the reaction and filter to remove excess catalyst.
[00...
Embodiment 2
[0049] On the basis of Example 1, the iron-zinc catalytic hydrogenation system also includes 2.5% chromium oxide.
[0050] Its ethylbenzene conversion rate is 90%
Embodiment 3
[0051] Embodiment 3 reduction system comparison
[0052] Adopt the reducing system and step parameter in embodiment 1, embodiment 2, only adjust temperature.
[0053] The optimized reaction temperature is 560°C, 570°C, and 580°C respectively, and the conversion rate of ethylbenzene is investigated
[0054] temperature (°C) 560, conversion rate of ethylbenzene 570, conversion rate of ethylbenzene 580, conversion rate of ethylbenzene Embodiment 1 reaction system of the present invention 80 83 75 Embodiment 2 reaction system of the present invention 85 92 80
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