Method and system for refining cyclohexanone and recycling cyclohexanol
A technology of cyclohexanol and cyclohexanone, which is applied in the field of cyclohexanone refining and cyclohexanol recycling, can solve the problem of high reaction activity, achieve the effects of high product purity, reduce material consumption and improve yield
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Specific embodiment one
[0031] A method for refining cyclohexanone and recycling cyclohexanol, such as figure 1 As shown, it specifically includes the following steps:
[0032] (1) The alcohol and ketone mixture (crude phenol hydrogenation product) containing cyclohexanone, cyclohexanol, light components and heavy components is sent to light removal tower 1, and the number of theoretical plates in light removal tower 1 is controlled to 30 -70 blocks, the pressure at the top of the tower is controlled at 40-65kpa, the reflux ratio is controlled at 100-1000, the light impurity components with cyclohexanone content less than 20wt% are extracted from the top of the light-removing tower 1, and the light component is extracted from the bottom of the tower Materials with sub-content less than 50ppm;
[0033] (2) Send the material with light component content lower than 50ppm obtained in step (1) to cyclohexanone product tower 2, control the theoretical plate number of cyclohexanone prod...
Example Embodiment
Specific embodiment two
[0040] The system used in the cyclohexanone refining and cyclohexanol recycling method in the above specific embodiment 1, such as figure 1 As shown, it includes light removal tower 1, cyclohexanone product tower 2, cyclohexanol recovery tower 3, cyclohexanol dehydrogenation reactor 4, gas-liquid separation tank 5, dehydration tower 6, oil-water separator 7, waste water collection tank 8. Cyclohexane extraction tower 9, alcohol and ketone recovery tower 10, the upper end of the light removal tower 1 is provided with an alcohol and ketone mixture material (crude phenol hydrogenation product) inlet 11, and the bottom material outlet of the light removal tower 1 and cyclohexanone product The middle material inlet of tower 2 is connected, the bottom material outlet of cyclohexanone product tower 2 is connected to the middle material inlet of cyclohexanol recovery tower 3, the bottom of cyclohexanol recovery tower 3 is provided with a heavy component outlet 1...
Example Embodiment
Specific embodiment three
[0042] The process method is the same as the first embodiment above, and the system equipment is the same as the second embodiment above. The differences are:
[0043] The number of theoretical plates in the light-removing tower 1 is 55, the top pressure is 55kpa, and the mass reflux ratio is 400;
[0044] The number of theoretical plates of the cyclohexanone product tower 2 is 55, the pressure at the top of the tower is 15 kpa, and the mass reflux ratio is 3;
[0045] The number of theoretical plates in the cyclohexanol recovery tower 3 is 45, the top pressure is 20 kpa, and the reflux ratio is 1.5;
[0046] The number of theoretical plates in the cyclohexane extraction tower 9 is 8, and the tower top pressure is 130 kpa;
[0047] The number of theoretical plates of the alcohol and ketone recovery tower 10 is 40, the pressure at the top of the tower is 105 kpa, and the mass reflux ratio is 0.8;
[0048] The dehydration tower 6 is a rectification tower, the num...
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