Tech. of preparing 2,4-di nitro methyl-phenoxide by nitro methyl-phenoxide continuous thermal insulating nitration
A technology of dinitroanisole and nitroanisole, which is applied in the preparation of nitro compounds, organic chemistry and other directions, can solve the problems of large discharge of waste water and waste residues, increase treatment costs, poor product quality, etc., and achieve production Low cost, reduced thermal energy, high reliability
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Embodiment 1
[0027] A kind of continuous adiabatic nitration of nitroanisole prepares 2,4-dinitroanisole technology, and described process step is as follows:
[0028] (1). Using 4-nitroanisole as a raw material, the mixed acid is prepared by mixing industrial grade 98% sulfuric acid, 95% nitric acid and 65% nitric acid. The dehydration value of the mixed acid is between 2.0 and 3.2. 4- The molar ratio of nitroanisole to nitric acid is 1:1.05, and a continuous adiabatic nitration reaction occurs in a continuous static mixer adiabatic nitration reactor, and the operating temperature is controlled between 65°C and 120°C.
[0029] (2). After the continuous adiabatic nitration reaction, the material is decompressed to 28.0KPa, the water and a small amount of nitric acid remaining in the nitration reaction are distilled off, and the waste acid is concentrated.
[0030] (3). After evaporating and concentrating, let stand for 1.0h, and carry out liquid-liquid layer separation. The lower water ph...
Embodiment 2
[0037] A kind of continuous adiabatic nitration of nitroanisole prepares 2,4-dinitroanisole technology, and described process step is as follows:
[0038] (1). Using 2-nitroanisole as a raw material, the mixed acid is prepared by mixing industrial-grade 98% sulfuric acid, 95% nitric acid and 65% nitric acid. The dehydration value of the mixed acid is between 2.8 and 4.2. 2- The molar ratio of nitroanisole to nitric acid is 1:1.05, and a continuous adiabatic nitration reaction occurs in a continuous static mixer adiabatic nitration reactor, and the operating temperature is between 65°C and 140°C.
[0039] (2). The material after the continuous adiabatic nitration reaction is decompressed to 78.0KPa to distill water and nitric acid left over from the nitration reaction, and concentrate the waste acid.
[0040] (3). After evaporating and concentrating, let stand for 0.5h, and carry out liquid-liquid layer separation. The lower water phase is sulfuric acid and a small amount of n...
Embodiment 3
[0047] A kind of continuous adiabatic nitration of nitroanisole prepares 2,4-dinitroanisole technology, and described process step is as follows:
[0048](1). The mixture of 2-nitroanisole and 4-nitroanisole is used as a raw material. The mixed acid is prepared by mixing industrial grade 98% sulfuric acid, 95% nitric acid and 65% nitric acid. The dehydration value of the mixed acid is Between 2.8 and 4.2, the molar ratio of nitroanisole and nitric acid is 1:1.05, continuous adiabatic nitration reaction occurs in continuous static mixer adiabatic nitration reactor, and the operating temperature is between 65°C and 140°C .
[0049] (2). The material after the continuous adiabatic nitration reaction is decompressed to 10.0KPa ~ 100KPa to distill water and nitric acid remaining from the nitration reaction, and concentrate the waste acid.
[0050] (3). After evaporating and concentrating, let stand for 0.5h, and carry out liquid-liquid layer separation. The lower water phase is s...
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