Device for preparing isopropyl acetate in heat pump dividing-wall reactive distillation column
A technology of isopropyl acetate and reactive distillation column, which is applied in the field of rectification, can solve the problems of high energy consumption, and achieve the effect of reducing energy consumption and saving equipment investment
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Embodiment 1
[0025] Attached figure 1In the process flow shown, the heat pump dividing wall reactive distillation column 1 used is a packed tower with a diameter of 800mm and 45 meters. The top separation area 2 is equipped with 5 meters of structured packing, and the number of theoretical plates is 10; the reaction separation area 3 is equipped with The structured packing is 35 meters, and the number of theoretical plates is 74, including 9 plates in the rectification section and 43 plates in the reaction section. The reaction section is filled with solid catalyst, the catalyst used is Amberlyst-15 strong acid cation exchange resin, and 12 plates in the stripping section plate. Methanol recovery area 4 is equipped with 5 meters of built-in structured packing, the operating pressure of heat pump partition wall reactive distillation column 1 is 1 atm, the top temperature of tower top separation area 2 is 54°C, the bottom temperature of reaction separation area 3 is 91°C, methanol recovery a...
Embodiment 2
[0028] Attached figure 1 In the process flow shown, the heat pump dividing wall reactive distillation column 1 used is a packed tower with a diameter of 800 mm and a height of 50 meters. There are 10 trays in the top separation area 2; the number of trays in the reaction separation area 3 is 76 Blocks, including 10 plates in the rectification section, 44 plates in the reaction section, filled with a solid catalyst in the reaction section, the catalyst used is Amberlyst-15 strongly acidic cation exchange resin, and 12 plates in the stripping section. There are 6 trays in the methanol recovery area 4, the operating pressure of the heat pump dividing wall reaction distillation column 1 is 2 atm, the top temperature of the tower top separation area 2 is 73 °C, the bottom temperature of the reaction separation area 3 is 113 °C, and the bottom of the methanol recovery area 4 The temperature is 83°C.
[0029] The raw material isopropyl alcohol is fed from the upper part of the react...
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