N-vinyl pyrrolidone purification system and method
A vinylpyrrolidone and purification method technology, applied in the field of N-vinylpyrrolidone preparation, can solve the problems of many reaction steps, environmental pollution, low production efficiency, etc., reduce the chance of self-polymerization of materials, reduce production costs, The effect of improving utilization efficiency
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Embodiment approach 1
[0107] figure 1 It is a schematic diagram of the NVP refining system and process flow according to Embodiment 1 of the present invention.
[0108] Such as figure 1 As shown, a kind of N-vinylpyrrolidone refining system comprises: the first rectifying unit 1, the first crystallization system 8 and the third rectifying unit 7 connected in series through the pipeline, the second rectifying unit 2 and the second rectifying unit connected in series The second crystallization system 9, and the NVP storage tank. Wherein, the first rectification unit 1 receives the synthetic reaction solution 00 containing NVP, carries out rectification treatment and outputs the first distillate 11 and the first still out 12, and the first crystallization system 8 receives the first distillate 11, carries out crystallization purification and outputs The first crystallization solution 81 and the first mother liquor 82, the third rectification unit 7 receives the first crystallization solution 81 and ...
Embodiment approach 2
[0117] figure 2 Schematic diagram of the NVP purification system and process flow according to Embodiment 2. The synthetic reaction solution 00 of NVP is prepared by the acetylene synthesis method. After gas-liquid separation, the synthetic reaction solution 00 comprises 30-55% (wt%) of NVP, 45-70% (wt%) of a-p, and 00 of the synthetic reaction solution. 960 liters / hour enters the first rectification unit 1 to carry out primary NVP purification (ie primary rectification purification). It is different from Embodiment 1 mainly in the following aspects:
[0118] Such as figure 2 As shown, the second rectification unit 2 of the NVP refining system includes two packed columns connected in sequence, that is, the fourth rectification tower 4 and the fifth rectification tower 5, and the fourth rectification tower 4 receives the first rectification unit 1 The first still goes out 12, carries out distillation purification, and outputs the 4th still and goes out 41 and the 4th still g...
Embodiment approach 3
[0122] image 3 Schematic diagram of the NVP purification system and process flow according to Embodiment 3. The synthetic reaction solution 00 of NVP is prepared by the acetylene synthesis method. After gas-liquid separation, the synthetic reaction solution 00 comprises 30-55% (wt%) of NVP, 45-70% (wt%) of a-p, and 00 of the synthetic reaction solution. 960 liters / hour enters the first rectification unit 1 to carry out primary NVP purification (ie primary rectification purification). It is different from Embodiment 2 mainly in the following aspects:
[0123] Such as image 3 As shown, the second rectification unit 2 of the NVP refining system also includes a third rectification tower 3, the third rectification tower 3 is arranged on the front end of the fourth rectification tower 4 and connected in series with it, and the third rectification tower 3 receives from The first still of the first rectification unit 1 goes out 12 and outputs the third still and goes out 31 and t...
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