AlSayed Ahmed, Soliman Moomen, ElDyasti Ahmed
Department of Civil Engineering, Lassonde School of Engineering, York University, ON, M3J1P3, Canada.
Department of Civil Engineering, Lassonde School of Engineering, York University, ON, M3J1P3, Canada.
J Environ Manage. 2023 May 15;334:117527. doi: 10.1016/j.jenvman.2023.117527. Epub 2023 Feb 18.
Nowadays, the shift toward energy and resource-efficient wastewater treatment plants (WWTPs) has become a necessity rather than a choice. For this purpose, there has been a restored interest in replacing the typical energy and resource-extensive activated sludge process with the two-stage Adsorption/bio-oxidation (A/B) configuration. In the A/B configuration, the role of the A-stage process is to maximize organics diversion to the solids stream and control the following B-stage's influent to allow for the attainment of tangible energy savings. Operating at very short retention times and high loading rates, the influence of the operational conditions on the A-stage process become more tangible than typical activated sludge. Nonetheless, there is very limited understanding of the influence of operational parameters on the A-stage process. Moreover, no studies in the literature have explored the influence of any operational/design parameters on the Alternating Activated Adsorption (AAA) technology which is a novel A-stage variant. Hence, this article mechanistically investigates the independent effect of different operational parameters on the AAA technology. It was inferred that solids retention time (SRT) shall remain below 1 day to allow for energy savings up to 45% and redirecting up to 46% of the influent's COD to the recovery streams. In the meantime, the hydraulic retention time (HRT) can be increased up to 4 h to remove up to 75% of the influent's COD with only 19% decline of the system's COD redirection ability. Moreover, it was observed that the high biomass concentration (above 3000 mg/L) amplified the effect of the sludge poor settleability either due to pin floc settling or high SVI which resulted in COD removal below 60%. Meanwhile, the concentration of the extracellular polymeric substances (EPS) was not found to be influenced or to influence process performance. The findings of this study can be employed to formulate an integrative operational approach in which different operational parameters are incorporated to better control the A-stage process and achieve complex objectives.
如今,向能源和资源高效型污水处理厂(WWTPs)转变已成为一种必然,而非一种选择。为此,人们重新燃起了用两阶段吸附/生物氧化(A/B)配置取代典型的能源和资源消耗型活性污泥工艺的兴趣。在A/B配置中,A阶段工艺的作用是使有机物最大限度地转移到固体流中,并控制后续B阶段的进水,以实现切实的节能效果。在非常短的停留时间和高负荷率下运行,操作条件对A阶段工艺的影响比典型的活性污泥工艺更为明显。尽管如此,人们对操作参数对A阶段工艺的影响了解非常有限。此外,文献中没有研究探讨任何操作/设计参数对交替活化吸附(AAA)技术的影响,而AAA技术是一种新型的A阶段变体。因此,本文从机理上研究了不同操作参数对AAA技术的独立影响。据推断,固体停留时间(SRT)应保持在1天以下,以实现高达45%的节能,并将高达46%的进水化学需氧量(COD)重定向到回收流中。与此同时,水力停留时间(HRT)可以增加到4小时,以去除高达75%的进水COD,而系统的COD重定向能力仅下降19%。此外,观察到高生物量浓度(高于3000mg/L)会因絮体沉降不佳或高污泥体积指数(SVI)而加剧污泥沉降性差的影响,导致COD去除率低于60%。同时,未发现胞外聚合物(EPS)的浓度对工艺性能有影响或受工艺性能影响。本研究的结果可用于制定一种综合操作方法,其中纳入不同的操作参数,以更好地控制A阶段工艺并实现复杂目标。