Method for synthesizing acetonitrile through one-step ammoniating method with acetic acid
A technology of acetic acid and acetonitrile, which is applied in the purification/separation of carboxylic acid nitriles, organic chemistry, ammonia-carboxylic acid reaction preparation, etc. It can solve the problems of difficult quality assurance, long process flow, and shortage of acetonitrile, and achieve fewer types of impurities, The separation process is simple and the process is short
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Embodiment 1
[0023] The internal structure and parameters of the fixed bed reactor are as follows:
[0024] Above is the raw material distributor, the raw material distributor is multi-tube type, the distribution pipes are vertically downward, and the distribution pipes are arranged in a square or equilateral triangle. The number of distribution pipes per square meter of the reactor cross section is 20, and the aperture is 3.8mm;
[0025] (1) Reaction:
[0026] Acetic acid and liquid ammonia are respectively vaporized and preheated to 360°C, and sent from the multi-tubular raw material distributor on the upper part of the reactor to a fixed-bed reactor equipped with catalyst aluminum oxide for reaction to generate a mixed gas containing acetonitrile The reaction temperature is 380°C, the pressure at the top of the reactor is 0.005MPa gauge pressure, the linear velocity of the empty bed is 0.8m / s, the ratio of the amount of acetic acid feed to the reactor, that is, the reaction weight hourl...
Embodiment 2
[0041] In the reaction process, acetic acid and liquid ammonia are respectively vaporized and preheated to 380°C; ammoniation reaction is at 400°C; the pressure at the top of the reactor is 0.060Mpa gauge pressure; the linear velocity of the empty bed is 0.7m / s; the reaction weight hourly space velocity WWH0.2h -1 ;
[0042] In the refining process, the reflux ratio at the top of the deamination tower is 5.0, and the operating pressure is 0.10Mpa; the top of the finished product tower adopts internal reflux, and the ratio of the reflux flow to the side line withdrawal is 3.0;
[0043] All the other parts are identical with embodiment 1.
[0044] The result of embodiment 2:
[0045] Acetic acid conversion ≥ 99%, yield ≥ 90%
[0046] The relative content of acetonitrile in the product is ≥90%
[0047] Purity of refined acetonitrile ≥99.9%
[0048] Raw material consumption: acetic acid: 1.5 tons / ton, ammonia 0.5 tons / ton
[0049] The catalyst cost is about 200 yuan / ton.
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