Device and method for cyclohexanone rectification
A technology for two towers of cyclohexanone and cyclohexanone, which is applied in the field of rectification devices of cyclohexanone, can solve the problems of increased energy consumption of the rectification system, the quality of product cyclohexanone cannot be stably controlled, and the like, and achieves reduction of steam consumption. and circulating water consumption, high product quality, good process stability
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Embodiment 1
[0045] like figure 1 As shown, the heterogeneous mixture of cyclohexanone / cyclohexanol enters the feed port 1-1 of the first light component tower, and the extracted material from the tower top 1-2 of the light component first tower enters the gas phase inlet 5 of the waste heat reboiler -1, after exchanging heat with the material in the tower kettle 2-2 of the first cyclohexanone tower, it is extracted from the condensate outlet 5-3 of the waste heat reboiler, and the uncondensed gas in the waste heat reboiler 5 is reboiled by waste heat The gas phase outlet 5-2 of the device enters the condenser 6 of the light component-tower 1, and the condensate produced by the condenser outlet 6-1 of the light component-tower 1 is extracted with the waste heat reboiler condensate outlet 5-3 After the condensate of the condensate is combined, enter the reflux port 1-3 of the first light component tower and the feed inlet 3-1 of the second light component tower respectively according to the...
Embodiment 2
[0050] like figure 1 As shown, the heterogeneous mixture of cyclohexanone / cyclohexanol enters the feed port 1-1 of the first light component tower, and the extracted material from the tower top 1-2 of the light component first tower enters the gas phase inlet 5 of the waste heat reboiler -1, after exchanging heat with the material in the tower kettle 2-2 of the first cyclohexanone tower, it is extracted from the condensate outlet 5-3 of the waste heat reboiler, and the uncondensed gas in the waste heat reboiler 5 is reboiled by waste heat The gas phase outlet 5-2 of the device enters the condenser 6 of the light component-tower 1, and the condensate produced by the condenser outlet 6-1 of the light component-tower 1 is extracted with the waste heat reboiler condensate outlet 5-3 After the condensate of the condensate is combined, enter the reflux port 1-3 of the light component first tower and the feed inlet 3-1 of the light component second tower respectively according to the...
Embodiment 3
[0055] like figure 1 As shown, the heterogeneous mixture of cyclohexanone / cyclohexanol enters the feed port 1-1 of the first light component tower, and the extracted material from the tower top 1-2 of the light component first tower enters the gas phase inlet 5 of the waste heat reboiler -1, after exchanging heat with the material in the tower kettle 2-2 of the first cyclohexanone tower, it is extracted from the condensate outlet 5-3 of the waste heat reboiler, and the uncondensed gas in the waste heat reboiler 5 is reboiled by waste heat The gas phase outlet 5-2 of the device enters the condenser 6 of the light component-tower 1, and the condensate produced by the condenser outlet 6-1 of the light component-tower 1 is extracted with the waste heat reboiler condensate outlet 5-3 After the condensate of the condensate is combined, enter the reflux port 1-3 of the light component first tower and the feed inlet 3-1 of the light component second tower respectively according to the...
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