膜
氨
化学
传质
废水
化学工程
剥离(纤维)
扩散
磁导率
润湿
渗透
分子扩散
色谱法
传质系数
焊剂(冶金)
膜透性
污水处理
膜技术
水处理
工作(物理)
过程(计算)
作者
Haoquan Zhang,Hou–Yong Yu,Zhan Wang,Yue Qing,Minyuan Han,Ye Jin,Le Han
标识
DOI:10.1021/acs.est.5c10757
摘要
The ammonia recovery from wastewater via a concentration-driven membrane stripping process is highly promising yet constrained by the trade-off issue between ammonia permeability and antiwettability of hydrophobic gas-permeable membranes (GPMs). We designated a tailored hierarchical-porous GPM (HGPM) via a facile fabrication method to address the above issue and established its transfer model, clearly illustrating the ammonia diffusion across the distinct layers. Molecular diffusion across the finger-like layer of HGPMs was responsible for a superior overall mass transfer coefficient of 3.3 × 10 –5 m/s. Meanwhile, its nanoscale pores in the top-skin and sponge-like layers conferred commendable wetting resistance against neighboring alkaline or acidic liquids, with the liquid entrance pressure measured at 182 kPa. The hierarchy of HGPMs together achieved the best-ever balance between ammonia permeability and antiwettability (both increased up to ∼150–200% of the commercial GPMs), significantly breaking the upper bound limit. Dealing with the real wastewater from anaerobic digestate, HGPMs demonstrated a robust ammonia recovery flux of 75–80 g N/m 2 h over 50 h, 3 times higher than that of the commercial GPMs. This work sheds light on the effective recovery of volatile valuable compounds from complex wastewater, with the as-tailored membrane of great upscalability holding great potential toward a future circular society.
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