Recovery process of caprolactam refining raffinate
A caprolactam and residual liquid technology, applied in extraction water/sewage treatment, oxidized water/sewage treatment, organic chemistry, etc., can solve the problems of polluted system, numerous processes, long preparation process, etc., to reduce unit consumption and increase annual output and economic effects
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Embodiment 1
[0015] Embodiment 1: the mass concentration of 647kg / h is 5% potassium permanganate aqueous solution in reactor and the caprolactam refining raffinate of 110kg / h carries out redox reaction under normal pressure, stirring state, and reaction temperature is controlled at 32 ~40°C, after the reaction is carried out for 30-40 minutes, the reactant is sent to another reactor to continue the reaction for 80-90 minutes under normal pressure and stirring, the reaction temperature is controlled at 78-82°C, and then the above-mentioned final redox product A total of 2757kg / h is sent to the extraction tower through the top, and is subjected to countercurrent extraction with 8271kg / h benzene extractant from the bottom of the tower. agent is the continuous phase. 10,000 kg / h of 20-21% caprolactam benzene solution obtained at the top of the tower is sent to the CPL device to recover caprolactam through water stripping, and about 1028 kg / h of the residual liquid at the bottom of the tower is...
Embodiment 2
[0016] Embodiment 2: the difference between this embodiment and embodiment 1 is that the benzene of 8271kg / h is the extractant, and the H of 5% is 647kg / h mass concentration 2 o 2 The aqueous solution is an oxidant, and the ratio of the redox product to the benzene extractant is 1:3.
Embodiment 3
[0017] Embodiment 3: the difference between this embodiment and embodiment 1 is that the toluene of 13785kg / h is the extractant, and the mass concentration of 647kg / h is 5% KMnO 4 The aqueous solution is an oxidant, and the ratio of the redox product to the toluene extractant is 1:5.
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