Method for preparing indole by oxidative dehydrogenation of o-ethylaniline
A technology of o-ethylaniline and oxidative dehydrogenation, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, organic chemistry, etc., can solve industrial application limitations, catalyst conversion rate and selectivity reduction , carbon on the surface of the catalyst, etc., to achieve the effect of convenient operation and reduction of reduction degree
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Embodiment 1
[0017] In the dehydrogenation reactor, fill 20 grams of boroaluminate copper catalysts, vaporize after o-ethylaniline and water are mixed and enter the fixed-bed reactor for reaction, the reaction temperature is 640 ° C, and the volume ratio of o-ethylaniline and water is 1: 6. The hourly space velocity of o-ethylaniline feed liquid is 0.1h -1 , After 200 h of normal pressure reaction, the conversion rate of o-ethylaniline and the selectivity of indole were measured, and the results are shown in Table 1.
Embodiment 2
[0019] Identical to the method of Example 1, the difference is that o-ethylaniline and water are mixed and then vaporized and then mixed with preheated air to enter the fixed-bed reactor for reaction. The mol ratio of o-ethylaniline and the oxygen in the air is 1:1, normal pressure reaction 200h after the measurement of o-ethylaniline conversion rate and indole selectivity, the results are shown in Table 1.
[0020] Table 1
[0021]
Embodiment 3
[0023] In the dehydrogenation reactor, fill 20 grams of copper boroaluminate catalyst, o-ethylaniline and water are mixed, vaporized and then mixed with preheated air, then enter the fixed bed reactor for reaction, the reaction temperature is 500 ° C, normal pressure, The volume ratio of o-ethylaniline and water is 1:6, the molar ratio of o-ethylaniline and oxygen is 1:1, and the hourly space velocity of o-ethylaniline liquid is 0.1h -1 , and the reaction results are shown in Table 2.
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Abstract
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