Method for recovery of organic waste gas by pressure swing adsorption of adsorption resin assisted by nitrogen purge
A technology of nitrogen purging and resin adsorption, which is applied in separation methods, chemical instruments and methods, and separation of dispersed particles. It can solve the problems of low regeneration efficiency, achieve small footprint, large volume adsorption capacity, and shorten operation time. Effect
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Embodiment 1
[0032] The main parameters for the treatment of ethyl acetate waste gas are: the air volume of the induced draft fan is 80CMH, and the intake concentration of ethyl acetate is 5g / m 3 , the intake air temperature is normal temperature, and the pressure is normal pressure. The diameter of the adsorber is DN=180mm, and the adsorbent is AMBERLITE TM For XAD4 resin, the filling height is H=300mm, the adsorption time is 90min, the vacuum desorption vacuum pumping time is 20min, and the vacuum is flushed into nitrogen every 5min for 1min, and the condenser uses 5°C frozen brine. The content of ethyl acetate in the exhaust gas after treatment is about 150mg / m 3 , 9.3Kg of ethyl acetate was recovered in 24h, and the recovery rate was 96.9%.
Embodiment 2
[0034] The desorption conditions in Example 1 were changed to vacuuming by a single vacuum pump without nitrogen purging, and other conditions remained unchanged. The content of ethyl acetate in the exhaust gas after treatment is about 730mg / m 3 , 8.2Kg of ethyl acetate was recovered in 24h, and the recovery rate was 85.4%.
Embodiment 3
[0036] Change the ethyl acetate gas in embodiment 1 to 5g / m 3 Toluene gas, other conditions remain unchanged. The content of toluene in the tail gas after treatment is about 170mg / m 3 , 9.48Kg of ethyl acetate was recovered in 24h, and the recovery rate was 98.8%.
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