State Key Laboratory of Heavy Oil Processing, Beijing Key Laboratory of Oil & Gas Pollution Control, China University of Petroleum, Beijing, 102249, China.
State Key Laboratory of Heavy Oil Processing, Beijing Key Laboratory of Oil & Gas Pollution Control, China University of Petroleum, Beijing, 102249, China.
Chemosphere. 2024 May;355:141834. doi: 10.1016/j.chemosphere.2024.141834. Epub 2024 Mar 31.
Membrane fouling caused by the organics-coated particles was the main obstacle for the highly efficient shale gas produced water (SGPW) treatment and recycling. In this study, a novel hybrid electrocoagulation (EC) and E-peroxone process coupled with UF (ECP-UF) process was proposed to examine the efficacy and elucidate the mechanism for UF fouling mitigation in assisting SGPW reuse. Compared to the TMP (transmembrane pressure) increase of -15 kPa in the EC-UF process, TMP in ECP-UF system marginally increased to -1.4 kPa for 3 filtration cycles under the current density of 15 mA/cm. Both the total fouling index and hydraulically irreversible fouling index of the ECP-UF process were significantly lower than those of EC-UF process. According to the extended Derjaguin-Landau-Verwey-Overbeek theory, the potential barriers was the highest for ECP-UF processes due to the substantial increase of the acid-base interaction energy in ECP-UF process, which was well consistent with the TMP and SEM results. Turbidity and TOC of ECP-UF process were 63.6% and 45.8% lower than those of EC-UF process, respectively. According to the MW distribution, the variations of compounds and their relative contents were probably due to the oxidation and decomposing products of the macromolecular organics. The number of aromatic compound decreased, while the number of open-chain compounds (i.e., alkenes, alkanes and alcohols) increased in the permeate of ECP-UF process. Notably, the substantial decrease in the relative abundance of di-phthalate compounds was attributed to the high reactivity of these compounds with ·OH. Mechanism study indicated that ECP could realize the simultaneous coagulation, HO generation and activation by O, facilitating the enhancement of ·OH and Al production and therefore beneficial for the improved water quality and UF fouling mitigation. Therefore, the ECP-UF process emerges as a high-efficient and space-saving approach, yielding a synergistic effect in mitigating UF fouling for SGPW recycling.
有机包裹颗粒引起的膜污染是高效页岩气采出水(SGPW)处理和回用的主要障碍。在这项研究中,提出了一种新型混合电絮凝(EC)和 E-peroxone 工艺与 UF(ECP-UF)工艺相结合的方法,以检验 UF 污染缓解在辅助 SGPW 再利用方面的效果,并阐明其机理。与 EC-UF 工艺中 TMP(跨膜压力)增加-15 kPa 相比,在电流密度为 15 mA/cm 时,ECP-UF 系统中的 TMP 在 3 个过滤循环中仅略微增加到-1.4 kPa。与 EC-UF 工艺相比,ECP-UF 工艺的总污染指数和水力不可逆污染指数均显著降低。根据扩展的德加古林-兰德瓦厄-奥弗贝克理论,由于 ECP-UF 工艺中酸碱相互作用能的大幅增加,ECP-UF 工艺的势垒最高,这与 TMP 和 SEM 结果非常吻合。ECP-UF 工艺的浊度和 TOC 分别比 EC-UF 工艺低 63.6%和 45.8%。根据 MW 分布,化合物的变化及其相对含量的变化可能是由于大分子有机物的氧化和分解产物。在 ECP-UF 工艺的渗透物中,芳香族化合物的数量减少,而开链化合物(即烯烃、烷烃和醇)的数量增加。值得注意的是,二邻苯二甲酸酯化合物的相对丰度大幅下降归因于这些化合物与·OH 的高反应性。机理研究表明,ECP 可以通过 O 实现同时混凝、HO 生成和活化,促进·OH 和 Al 的产生,从而有利于提高水质和减轻 UF 污染。因此,ECP-UF 工艺是一种高效、节省空间的方法,在减轻 SGPW 回收过程中的 UF 污染方面具有协同作用。