Method and device for preparing caprolactam through cyclohexanone oxime rearrangement reaction
A technology of cyclohexanone oxime and rearrangement reaction is applied in the field of chemical product production to achieve the effects of high energy efficiency, improved mass transfer and optimized reaction conditions
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Embodiment 1
[0025] The hot solvent is chloroform, the cyclohexanone oxime, chloroform, and the amidation liquid containing concentrated sulfuric acid or fuming sulfuric acid enter the cyclohexanone oxime inlet 11, the hot solvent inlet 10 and the amidation liquid inlet 14 respectively into the third The liquid phase mixer 5 performs mixing, and then enters the supergravity reactor 8 to continue mixing. The volume ratio of chloroform and cyclohexanone oxime is 6:1, the acid oxime ratio of the mixed liquid after mixing is 1.3:1 (molar ratio), the rotor speed of the supergravity reactor is 2000 rpm, and the mixing temperature is 65°C. The mixed liquid passes through the supergravity reactor liquid outlet 3 to the subsequent rearrangement reactor 13 for further rearrangement reaction. The rearrangement reaction temperature is 71°C, the system pressure is 0.04MPa, and the subsequent rearrangement reaction stirrer revolutions is 500 Rpm. The materials leaving the subsequent rearrangement react...
Embodiment 2
[0027] The hot solvent is heptane, the volume ratio of heptane to cyclohexanone oxime is 10:1, the acid oxime molar ratio of the mixed solution after mixing is 0.9:1, and the rotor speed of the high gravity reactor 8 is 500 rpm , The mixing temperature is 70℃. The material leaving the supergravity reactor enters the subsequent rearrangement reactor 13 for further rearrangement reaction, the reaction temperature is 110°C, and the pressure is 0.25Mpa. The materials leaving the subsequent rearrangement reactor undergo crystallization, neutralization, extraction and purification processes to obtain caprolactam. The conversion rate of cyclohexanone oxime was 90%, and the selectivity of caprolactam was 88.7%.
Embodiment 3
[0029] The hot solvent is petroleum ether, the volume ratio of petroleum ether to cyclohexanone oxime is 18:1, the molar ratio of acid oxime is 1.2:1, the speed of the rotor of the supergravity reactor is 1200 rpm, and the mixing temperature is 65°C . The materials leaving the supergravity reactor flow into the subsequent rearrangement reactor 13 for further rearrangement reaction, the reaction temperature is 65°C, and the system pressure is 0.001Mpa. The materials leaving the subsequent rearrangement reactor undergo crystallization, neutralization, extraction and purification processes to obtain caprolactam. The conversion rate of cyclohexanone oxime was 100%, and the selectivity of caprolactam was 99.8%.
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