Novel method for rectifying and separating acetone and isopropyl ether systems under variable pressures
A technology of pressure swing rectification and isopropyl ether, which is applied in the separation/purification of ether, separation/purification of carbonyl compounds, preparation of ether, etc. It can solve the problems of large amount of extractant, complex process, high energy consumption, etc., and achieve the reduction of separation cost, solving separation difficulties, and improving the effect of product purity
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Embodiment 1
[0050] Feed flow rate is 1000kg / h, temperature is 30°C, pressure is 6atm (absolute pressure), mass composition: acetone 60%, isopropyl ether 40%. The number of theoretical plates in the high pressure column (HT) is 40, and the material is fed to the 20th plate. The recycle stream is fed to the 11th plate of the high pressure column (HT). ℃. The low pressure column (LT) has 20 theoretical plates, feeds in the twelfth block, the reflux ratio is 1, the temperature at the top of the tower is 15°C, and the temperature at the bottom of the tower is 55°C.
[0051] After separation: the acetone product quality purity reaches 99.8%; the isopropyl ether product quality purity reaches 99.82%; the yield of acetone reaches 99.89%; the yield of isopropyl ether reaches 99.85%.
Embodiment 2
[0053] Feed flow rate is 1000kg / h, temperature is 30°C, pressure is 1atm (absolute pressure), mass composition: acetone 70%, isopropyl ether 30%. The number of theoretical plates in the high-pressure tower (HT) is 40, and the feed is at the 28th plate. The recycle stream is fed at the 13th plate of the high-pressure tower (HT). The reflux ratio is 1.5. ℃. The low-pressure column (LT) has 20 theoretical plates, feeds to the 8th block, the reflux ratio is 1.5, the temperature at the top of the tower is 20°C, and the temperature at the bottom of the tower is 50°C.
[0054] After separation: the acetone product quality purity reaches 99.99%; the isopropyl ether product quality purity reaches 99.99%; the yield of acetone reaches 99.9%; the yield of isopropyl ether reaches 99.92%.
Embodiment 3
[0056] Feed flow rate is 1000kg / h, temperature is 30°C, pressure is 1atm (absolute pressure), mass composition: acetone 85%, isopropyl ether 15%. The theoretical plate number of the high pressure column (HT) is 40, and the feed is at the 26th plate, and the recycle stream is fed at the 10th plate of the high pressure column (HT), the reflux ratio is 2.5, the temperature at the top of the tower is 110°C, and the temperature at the bottom of the tower is 130°C ℃. The low-pressure column (LT) has 20 theoretical plates, feeds at the tenth block, the reflux ratio is 1, the temperature at the top of the tower is 25°C, and the temperature at the bottom of the tower is 60°C.
[0057] After separation: the acetone product quality purity reaches 99.92%; the isopropyl ether product quality purity reaches 99.9%; the yield of acetone reaches 99.8%; the yield of isopropyl ether reaches 99.82%.
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