Propylene recovery device
A technology of propylene and equipment, which is applied in the field of equipment for recovering propylene from propylene epoxidation reaction products, can solve the problem of high energy consumption, and achieve the effect of reducing the amount of feed and reducing energy consumption
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Embodiment 1
[0025] Such as figure 1 As shown, taking a 100,000-ton / year PO plant as an example, the raw materials containing α,α-dimethylbenzyl alcohol, cumene, propylene oxide, propylene and propane from the epoxidation reaction system pass through the pipeline 11 first It is sent to the high-pressure propylene recovery tower 1 for separation, the top of the tower obtains the first light component stream, and the tower bottom obtains the first recombination containing α,α-dimethylbenzyl alcohol, cumene, propylene oxide, a small amount of propylene and propane Sub-logistics. The first heavy component stream is sent to the low pressure propylene recovery tower 2 for separation, the second light component stream is obtained at the top of the tower, and the crude propylene oxide product stream from which propylene is removed is obtained from the tower bottom. The propylene stream recovered at the top of the low-pressure propylene recovery tower 2 is divided into two parts, a part of which en...
Embodiment 2
[0034] Same as [Example 1], except that the raw materials and operating conditions are changed.
[0035] In the raw materials, in terms of weight percentage, 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%, and the content of propane is The content is 2%.
[0036] The operating conditions of the high-pressure propylene recovery tower are: the operating pressure is 1.6MPa, the operating temperature at the top of the tower is 40°C, the operating temperature of the tower bottom is 87°C, and the number of theoretical plates is 25.
[0037] The operating conditions of the low pressure propylene recovery tower are as follows: operating pressure is 0.2MPa, tower top operating temperature is -20°C, tower bottom operating temperature is 120°C, and the number of theoretical plates is 20.
[0038] The operating conditions of the de-propanizer are as follows: operating pressure is 2.0MPa, op...
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