Preparing method of low-carbon nitroparaffins
A technology for nitroalkane and nitropropane, which is applied in the field of safe gas-phase nitration to obtain nitroalkane with specific selectivity, can solve the problem that the specific selectivity of nitrification products cannot be completely solved.
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Embodiment 1
[0017] The invention adopts a multi-channel reactor to carry out the nitrification reaction. The molar ratio of propane and nitric acid is 6:1, and the operating pressure is 0.1Mpa. Propane enters the reaction channel port through the flowmeter, and nitric acid is pumped into the reaction channel port through the metering pump. The materials are fully mixed in the mixing chamber and then enter the reactor. The reaction temperature is 340 °C, residence time 0.8s, continuous reaction for 1h, the product flows out from the outlet after being condensed in the collection chamber, the obtained product is separated, the upper layer is an organic phase, and the lower layer is an aqueous phase. The upper layer was analyzed by gas chromatography, and the selectivities of the four nitro compounds were 4.4% for nitromethane, 11% for nitroethane, 41.6% for 1-nitropropane, and 44% for 2-nitropropane.
Embodiment 2
[0019] The process and the reactor used are the same as in Example 1, except that the molar ratio of propane to nitric acid is 2:1, the operating pressure is 0.5Mpa, and the residence time is 1.4s. The selectivities of the four nitro compounds were 6.7% for nitromethane, 12.2% for nitroethane, 42% for 1-nitropropane, and 39.1% for 2-nitropropane.
Embodiment 3
[0021] The process and the reactor used are the same as in Example 1, except that the reaction temperature is 435°C. The selectivities of the four nitro compounds were 7% for nitromethane, 13% for nitroethane, 45% for 1-nitropropane, and 35% for 2-nitropropane.
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