| Literature DB >> 31901775 |
Rui Du1, Shenbin Cao2, Xiangchen Li1, Jincheng Wang1, Yongzhen Peng3.
Abstract
Partial denitrification (PD, NO3--N → NO2--N) provides a promising opportunity for anammox application in wastewater nitrogen removal. In this study, a continuous-flow PD/Anammox (PD/A) process operated with a novel gas mixing was reported in an up-flow anaerobic bed reactor. A high nitrogen removal rate of 2.42 kgN/(m3∙d) was achieved at a relatively short hydraulic retention time (HRT) of 0.5 h with both influent NH4+-N and NO3--N of 30 mg/L. Sludge floatation was eliminated by mixing with gas of the reactor due to an efficiently improved mass transfer. Further optimization of gas flowrates at high NLR could avoid the overproduction of tight-bound extracellular polymeric substances (TB-EPS) and benefit sludge stability. Functional microorganisms of PD and anammox were effectively retained, and Zoogloea affecting sludge settleability kept increasing throughout the operation. This study clearly demonstrated the effectiveness of gas mixing strategy for a high-rate continuous-flow PD/A process with stable nitrogen removal performance.Entities:
Keywords: Anammox; Gas mixing; Partial-denitrification; Sludge flotation; Upflow anaerobic bed reactor (UASB)
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Year: 2019 PMID: 31901775 DOI: 10.1016/j.biortech.2019.122675
Source DB: PubMed Journal: Bioresour Technol ISSN: 0960-8524 Impact factor: 9.642