Method for separating perfluoroalkylethylene from perfluoroalkyl ethyl acrylate crude product
A technology of perfluoroalkyl ethyl acrylate and perfluoroalkyl ethylene, which is applied in the field of separation and recovery of perfluoroalkyl ethylene, can solve the problems of complex treatment process and high energy consumption, and achieve the effect of improving utilization efficiency and reducing emissions
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Embodiment 1
[0034] (1) Flow the liquid phase material in the 100Kg perfluoroalkyl ethyl acrylate reactor through the pipeline to the filter, and place 108Kg of the obtained filtrate in the rectification tower, and the operating pressure in the tower is about 20KPa, Collect 38Kg of solvent crude fraction at 40-80°C, 6Kg of perfluoroalkylethylene crude fraction at 90-110°C, and 64Kg of perfluoroalkyl ethyl acrylate crude fraction as the bottom material.
[0035] (2) Place the perfluoroalkylethylene crude fraction obtained in step (1) in a washing tank, add a KOH solution with a mass percent concentration of 5% to it at a rate of 5Kg / min for washing (the amount of KOH solution is about 10Kg ) with constant stirring. After the lye washing is finished, add deionized water to it at a certain speed for washing until it is neutral (the amount of deionized water is about 15Kg).
[0036] (3) Add 50 g of activated alumina powder (40 mesh) to the crude fraction of perfluoroalkylethylene obtained in ...
Embodiment 2
[0040](1) Flow the liquid phase material in the 100Kg perfluoroalkyl ethyl acrylate reactor to the filter 2 through the pipeline, and place 112Kg of the obtained filtrate in the rectification tower, and the operating pressure in the tower is about 30KPa , respectively collected 45Kg of solvent crude fraction at 40-60°C, 6.2Kg of perfluoroalkylethylene crude fraction at 90-100°C, and 60.8Kg of perfluoroalkyl ethyl acrylate crude fraction as the bottom material.
[0041] (2) Put the solvent crude fraction obtained in step (1) in a rectification tower, the operating pressure in the tower is about 20KPa, collect 42Kg of the solvent crude fraction at 40-60°C, and the tower bottom material mainly contains perfluoroalkyl The crude fraction of ethyl acrylate crude fraction 3Kg;
[0042] (3) Put the crude fraction of perfluoroalkyl ethyl acrylate obtained in step (1) in a rectification tower, the operating pressure in the tower is about 20KPa, and the rectification temperature is 90°C....
Embodiment 3
[0047] (1) Flow the liquid phase material in the 100Kg perfluoroalkyl ethyl acrylate reaction kettle to the filter 2 through the pipeline, and place 110Kg of the obtained filtrate in the rectification tower, and the operating pressure in the tower is about 40KPa , respectively collected 45Kg of solvent crude fraction at 40-90°C, 6.2Kg of perfluoroalkylethylene crude fraction at 90-110°C, and 58.8Kg of perfluoroalkyl ethyl acrylate crude fraction as the bottom material.
[0048] (2) Place the solvent crude fraction obtained in step (1) in a rectification tower, the operating pressure in the tower is about 40KPa, collect 41.5Kg of the solvent crude fraction at 40-90°C, and the tower bottom material mainly contains perfluoroalkane Crude distillate 3.5Kg of ethyl ethyl acrylate;
[0049] (3) Put the crude fraction of perfluoroalkyl ethyl acrylate obtained in step (1) in a rectification tower, the operating pressure in the tower is about 40KPa, and the rectification temperature is ...
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