Zhang Na, Zeng Xiang-Li, Liao Wen-Wei, Chen Meng-Yi, Zhang Guijiao, Ren Da-Heng, Ba Xu-Chen, Zhang Min-Kun, Xu Hao-Ran, Wang Aijie, Cheng Hao-Yi
State Key Laboratory of Urban Water Resources and Environment, School of Eco-Environment, Harbin Institute of Technology Shenzhen, Shenzhen 518055, China.
State Key Laboratory of Urban Water Resources and Environment, School of Environment, Harbin Institute of Technology, Harbin 150090, China.
Water Res. 2025 Sep 1;283:123882. doi: 10.1016/j.watres.2025.123882. Epub 2025 May 21.
Using powdered sulfur (S) with high specific surface area enables high efficiency in an elemental sulfur-based denitrification (ESDeN) reactor but faces challenges with S retention. While integrating the ESDeN process with microfiltration membranes (MM) has been shown to effectively reject S powder, severe membrane fouling and high membrane costs restrict its practical application. This study, for the first time, reports a dynamic membrane-equipped ESDeN (ESDeN-DM) reactor. The DM was formed by in-situ pre-coating a solid mixture (particle size: 0.4 μm to 110 μm) of S powder and denitrifying sludge onto inexpensive nylon fabrics. Initially, we optimized the DM formation conditions, determining that a nylon fabric pore size of 25 μm and a pre-coating flux of 300 L m² h resulted in permeate turbidity lower than 5 NTU within 60 mins. Subsequently, we identified the duration (12.5 days) of a transmembrane pressure (TMP)-dependent run (≤30 KPa) for the reactor and found that the TMP increase was related to the thickening and densification of the cake layer. Finally, we conducted a comparative examination of the ESDeN-DM reactor and the conventional ESDeN-MM reactor during long-term operation. The results demonstrated that the ESDeN-DM reactor achieved a comparable denitrification rate to the ESDeN-MM reactor (both with the maximum value more than 3 kg N m⁻ d⁻¹) but exhibited significantly better membrane fouling tolerance (56 % longer TMP-dependent run time), easier regeneration of specific flux (online backwash versus offline chemical cleaning), and exceptional cost-effectiveness (over 90 % total cost reduction). This study presents a highly efficient and easily maintained membrane-equipped ESDeN process with great potential for treating high-nitrate industrial wastewater.
使用具有高比表面积的粉状硫(S)可在基于元素硫的反硝化(ESDeN)反应器中实现高效,但面临硫保留的挑战。虽然将ESDeN工艺与微滤膜(MM)集成已被证明能有效截留硫粉,但严重的膜污染和高昂的膜成本限制了其实际应用。本研究首次报道了一种配备动态膜的ESDeN(ESDeN-DM)反应器。动态膜是通过将硫粉和反硝化污泥的固体混合物(粒径:0.4μm至110μm)原位预涂覆在廉价的尼龙织物上形成的。最初,我们优化了动态膜的形成条件,确定尼龙织物孔径为25μm且预涂覆通量为300 L m² h时,60分钟内渗透液浊度低于5 NTU。随后,我们确定了反应器跨膜压力(TMP)依赖运行(≤30 KPa)的持续时间(12.5天),并发现TMP的增加与滤饼层的增厚和致密化有关。最后,我们在长期运行期间对ESDeN-DM反应器和传统的ESDeN-MM反应器进行了对比研究。结果表明,ESDeN-DM反应器实现了与ESDeN-MM反应器相当的反硝化速率(两者最大值均超过3 kg N m⁻ d⁻¹),但表现出明显更好的膜污染耐受性(TMP依赖运行时间长56%)、特定通量更容易再生(在线反冲洗与离线化学清洗)以及卓越的成本效益(总成本降低超过90%)。本研究提出了一种高效且易于维护的配备膜的ESDeN工艺,在处理高硝酸盐工业废水方面具有巨大潜力。