Propylene recovery method
A technology for propylene and recovery towers, which can be used in chemical instruments and methods, purification/separation of hydrocarbons, hydrocarbons, etc., and can solve the problem of high energy consumption
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Embodiment 1
[0026] Such as figure 1 As shown, taking a 100,000-ton / year PO plant as an example, the raw material 11 containing α,α-dimethylbenzyl alcohol, cumene, propylene oxide, propylene and propane from the epoxidation reaction system is first sent to The high-pressure propylene recovery tower 1 is used for separation, and a stream 4 is obtained from the top of the tower, and a stream 5 containing α,α-dimethylbenzyl alcohol, cumene, propylene oxide, a small amount of propylene and propane is obtained from the bottom of the tower. Stream 5 is sent to low-pressure propylene recovery tower 2 for separation, stream 6 is obtained at the top of the tower, and crude propylene oxide product stream 8 for removing propylene is obtained in the tower reactor. The overhead stream 6 of the low-pressure propylene recovery tower 2 is divided into two parts, and a part of the stream 7 enters the depropanizer. After separation, the stream 9 is obtained at the top of the tower, and the propane stream 10...
Embodiment 2
[0035] With [embodiment 1], just raw material and operating condition change.
[0036] In the raw material, by weight percent, the content of α,α-dimethylbenzyl alcohol is 26%, the content of cumene is 21.5%, the content of propylene oxide is 10.5%, the content of propylene is 39%, the content of propane The content is 2%.
[0037] The operating conditions of the high-pressure propylene recovery tower are as follows: the operating pressure is 1.6MPa, the operating temperature at the top of the tower is 40°C, the operating temperature at the bottom of the tower is 87°C, and the number of theoretical plates is 25.
[0038] The operating conditions of the low-pressure propylene recovery tower are as follows: the operating pressure is 0.2 MPa, the operating temperature at the top of the tower is -20°C, the operating temperature at the bottom of the tower is 120°C, and the number of theoretical plates is 20.
[0039] The operating conditions of the depropanizer are as follows: the...
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