High-selectivity acetonitrile preparation method
A technology selected from acetonitrile, applied in the field of organic matter preparation, to achieve the effect of low cost
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Embodiment 1
[0037] In this example, a quartz tubular reactor with a diameter of 10 mm and a length of 250 mm was used. In the reactor, the catalyst was supported by quartz wool. Install the quartz reactor in a temperature-controlled furnace. Reactor temperature was monitored by thermocouples inserted into the surface of the temperature-controlled furnace packed bed. During operation, use NH 3 , NH 3 / N 2 or NH 3 / He mixed gas is used as the carrier gas, and its flow rate is controlled by a gas flow meter. The powdery raw materials flow together with the carrier gas flow from the opening of the quartz tube to the pyrolysis interface. The reaction temperature is 200-900°C, and the carrier gas flow rate is 5-200mL / min. Liquid products flow from the reactor to the condenser and gaseous products are collected in gas sampling bags. Liquid and gaseous products were analyzed using a gas chromatograph.
[0038] As representative of several embodiments, the catalytic pyrolysis tests descri...
Embodiment 2
[0041] In this example, the preparation of acetonitrile by catalytic pyrolysis of different raw materials such as chlorella, spirulina, lysine, aspartic acid, duckweed, rapeseed cake, and activated sludge was tested.
[0042]
[0043]
[0044] Reaction conditions: the reaction temperature is 800° C.; the catalyst is ZSM-5; the flow rate of ammonia gas is 40 mL / min. Example 3:
Embodiment 3
[0045] In this embodiment, the influence of different reaction temperatures on the yield and selectivity of acetonitrile was tested.
[0046]
[0047] Reaction conditions: the raw material is chlorella; the catalyst is ZSM-5; the flow rate of ammonia gas=40mL / min.
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