4-nitro-o-xylene continuous synthesis system and synthesis method
A technology of nitro-o-xylene and nitrification system, which is applied in the continuous synthesis system and synthesis field of 4-nitro-o-xylene, can solve the problems of poor selectivity of the target product of nitration reaction, many waste acids and inability to recycle, etc. The effect of reducing standing time and equipment volume, sufficient heat exchange area and good stirring
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Embodiment 1
[0066] Ortho-xylene and nitric-sulfur mixed acid are put into the mixer from their respective high-level tanks through the metering pump, wherein, in the nitric-sulfur mixed acid, the molar ratio of nitric acid to sulfuric acid is 1:0.5-1; the molar amount of nitric acid in the nitric-sulfur mixed acid Calculated, the molar ratio of o-xylene and nitric acid mixed acid is 1:1.5-2. After mixing o-xylene and nitric-sulfur mixed acid in the mixer, nitrogen is pressed into the double-ring nitration reactor, and the feed flow rate of the ortho-xylene and nitric-sulfur mixed acid mixture is 1.5-2m / s. The mixed material is pressed into the nitration system, and the organic phase and the acid phase are fully contacted to carry out multi-stage nitration reaction. The temperature in the ring-shaped nitration reactors at all levels is controlled at 10-25°C by means of heat exchangers.
[0067] The reaction solution flows out of the nitrification system and enters the first phase-separati...
Embodiment 2
[0070] Ortho-xylene and nitric-sulfur mixed acid are put into the mixer from their respective high-level tanks through the metering pump, wherein, in the nitric-sulfur mixed acid, the molar ratio of nitric acid to sulfuric acid is 1:0.1-0.44; the molar amount of nitric acid in the nitric-sulfur mixed acid Calculated, the molar ratio of o-xylene and nitric acid mixed acid is 1:1.1-2. After mixing o-xylene and nitric-sulfur mixed acid in the mixer, nitrogen is pressed into the double-ring nitration reactor, and the feed flow rate of the ortho-xylene and nitric-sulfur mixed acid mixture is 1.5-2m / s. The mixed material is pressed into the nitration system, and the organic phase and the acid phase are fully contacted to carry out multi-stage nitration reaction. The temperature in the annular nitration reactors at all levels is controlled to be 10-15° C. through heat exchangers.
[0071] The reaction solution flows out of the nitrification system and enters the first phase-separati...
Embodiment 3
[0074] Compared with Example 2, the washing system is a single-stage labyrinth washing tank. After the continuous production ends, the conversion rate of o-xylene is 90%. , sampling once every 30min), the content of 4-nitro-o-xylene is greater than 91%, and the purity of the 4-nitro-o-xylene collected by rectification is greater than 99.6% (GC area normalization method purity).
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