基于流态化作用的吸附反应动力学和穿透特征

基于流态化作用的吸附反应动力学和穿透特征研究还鲜见报道.以苯酚为吸附质、活性炭为吸附剂,探讨了不同流态化紊流强度对基于流态化作用的吸附效率、吸附动力学特性、吸附反应穿透曲线和饱和吸附量的影响,并与相同条件的固定床吸附反应器进行了对比研究.结果表明,表观流速为8 mm·s-1和13 mm·s-1时,基于流态化和固定态的活性炭在5 min内的吸附效率均达到93%以上,吸附反应均符合经典二级动力学方程,且其相关系数大于0.999.穿透实验结果表明,表观流速为6 mm·s-1和8 mm·s-1时,基于流态化的活性炭对苯酚的吸附总量分别较固定态高8.77 mg·g-1和24.70 mg·g-1.可见,基于流态化吸附反应器与基于固定态吸附反应器相比,具有吸附反应效率高,吸附总量大的特征.

Adsorption Dynamics and Breakthrough Characteristics Based on the Fluidization Condition

Few studies on the adsorption dynamics and breakthrough characteristics based on the fluidization condition have been reported. In a fluidized bed adsorption reactor with phenol as the adsorbate and granular activated carbon as the adsorbent, the adsorption efficiency, adsorption dynamic characteristics, adsorption breakthrough curves and adsorption capacities were studied and compared with those of a fixed bed operated under the same conditions. The results showed that the adsorption efficiencies exceeded 93% in 5 min in both the fluidized conditions and fixed conditions at the superficial velocities of 8 mm·s^-1 and 13 mm·s^-1. Meanwhile, the above adsorption reactions fitted to Pseudo-second-order with linear correlation coefficients greater than 0.999. The adsorption capacity of fluidized conditions was 8.77 mg·g^-1 and 24.70 mg·g^-1 at the superficial velocities of 6 mm·s^-1 and 8 mm·s^-1. Generally, the fluidized bed reactor showed a higher adsorption efficiency and greater adsorption capacity than the fixed bed reactor.