Ozone micro-bubble aeration using the ceramic ultrafiltration membrane with superior oxidation performance for 2, 4-D elimination

曝气 气泡 臭氧 陶瓷膜 化学 降级(电信) 超滤(肾) 化学工程 环境工程 陶瓷 色谱法 有机化学 环境科学 工程类 电信 并行计算 生物化学 计算机科学
作者
Wei-Ran Han,Wenlong Wang,Tiejun Qiao,Wei Wang,Hang Su,Chen-Xin Xu,Qian-Yuan Wu
出处
期刊:Water Research [Elsevier BV]
卷期号:237: 119952-119952 被引量:28
标识
DOI:10.1016/j.watres.2023.119952
摘要

Micro-bubble aeration is an efficient way to promote ozonation performance, but the technology is challenged by extensive energy cost. Here, a ceramic ultrafiltration membrane was used to achieve ozone micro-bubble (0–80 µm) aeration in a simple way at gaseous pressures of 0.14–0.19 MPa. Compared with milli-bubble aeration, micro-bubble aeration increased the equilibrium aquatic O3 concentrations by 1.53–3.25 times and apparent O3 transfer rates by 3.12–3.35 times at pH 5.0–8.0. Consequently, the •OH yield was 2.67–3.54 times via faster O3 transfer to the aquatic solution followed by decomposition rather than interfacial reaction. Ozone micro-bubble aeration outperformed milli-bubble aeration, with the degradation kinetics of 2,4-D being 3.08–4.36 times higher. Both O3-oxidation and •OH oxidation were important to the promotion with the contributions being 35.8%-45.9% and 54.1%-64.2%, respectively. The operational and water matric conditions influenced the oxidation performance via both O3 oxidation and •OH oxidation, which is reported for the first time. In general, the ceramic membrane offered a low-energy approach of ozone micro-bubble aeration for efficient pollutant degradation. The O3 oxidation and •OH oxidation were proportionally promoted by ozone micro-bubble due to O3 transfer enhancement. Thus, the promotive mechanism can be interpreted as the synchronous enchantment on ozone exposure and •OH exposure for the first time.
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