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TSS concentration in both reactors during the experiment

TSS concentration in both reactors during the experiment

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The anammox process is an economically favourable nitrogen removal process; however, low growth rates of anammox biomass block its more widespread application. As different approaches on techniques for anammox bacteria growth acceleration were tested, this study focused on long-term evaluation of hydrazine addition in the start-up phase. Effect of...

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... initial NRR during stabilization period (until day 6) was 0. 034 Fig. 1b, c). During this phase, in both reactors, average dissolved oxygen concentration was kept Fig. 1 a NH 4 -N, NO 2 -N, and NO 3 -N concentration in the influent medium. b NH 4 -N, NO 2 -N, and NO 3 -N concentration in the R1 effluent and c NH 4 -N, NO 2 -N, and NO 3 -N concentration in the R2 effluent at very low level to prevent potential inhibition: 0.03 ± 0.02 (max. 0.12) gO 2 m −3 and 0.03 ± 0.02 (max. 0.11) gO 2 m −3 for R1 and R2, respectively. ...
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... 1:523 | https://doi.org/10.1007/s42452-019-0514-4 Research Article potential estimation of share of anammox biomass in the VSS fraction is impossible due to scale of the experimental reactor where biofilm removal from reactor and used equipment was not possible. That situation explained why NLR and NRR was growing with no change of TSS of biomass (Fig. 4). Participation Anammox biomass in sludge was small and growth of that organism was impossible to measured by regular TSS measurement method. For more accurate evaluation of hydrazine addition effect in a long-term experiment, an alternative method for anammox growth rate estimation must be used, similar to activated sludge procedure ...

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... Introducing pyrrhotite (FeS) accelerated AnAOB growth in 18 days, surpassing 96 % TNRE in a lab UASB system [115]. Conversely, Miodoński et al. [116] used 3.7 mg/L of N 2 H 4 for rapid anammox initiation in a pilot SBR for sidestream wastewater treatment. This dosage was maintained over 36 days, resulting in an NRR of 0.519 g/L/d of N. ...
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... Particularly, the slow growth rate of anammox bacteria, with a doubling time of approximately 7-20 days, makes biomass concentration a critical factor for successful start-up and stable operation of the anammox process [5]. While various approaches, including the use of carriers for anammox bacteria growth [6] and the addition of specific elements to enhance their growth [7], have been explored to maintain biomass concentrations, an efficient operational strategy is still needed to achieve rapid start-up, reduce biomass washout, and obtain high biomass yield [8]. ...
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... Hydrazine, an additional exogenous substance, helps enrich anammox bacteria in the anammox process by having a role in bacterial growth. The hydrazine addition facilitates an anammox bacterial enrichments along with enhanced nitrogen removal efficiency (0.512 kg N (m 3 d -1 ) Vs 0.256 kg N (m 3 d -1 ), control [56]. The presence of hydrazine in anammox systems facilitates the increased NH 4 + -N oxidation rates and decreased NO 2 --N reduction rate by affecting the nitrite-oxidizing bacteria activity with the simultaneous enhancement of anammox bacterial growth.The positive results with the exogenous hydrazine addition on the anammox process led to testing the other substances, such as acyl homoserine-lactones(AHLs). AHLs are mediator molecules in quorum sensing, a bacterial cell-to-cell interaction process.The enhanced anammox results with the addition of AHLs were reported in several instances where the concentration above the threshold value of AHLs triggers the respective genes with their specific phenotypes such as anchorage, activity, granulation of the anammox biomass.The addition of AHL in a CSTR-driven anammox process facilitates a 17.5% lesser startup time compared with a reference process [57]. ...
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... Due to the extremely long doubling time of anammox bacteria (7-20 days) (Kartal et al. 2012), challenging start-up period of the process is one of the main obstacles. Therefore, in order to shorten the start-up time of the Anammox process, many researchers have focused on optimizing key parameters such as seeding sludge, operational strategy, biomass immobilization, etc. (Verma et al. 2021), and the addition of chemical reagents into the system for stimulating the bacteria (Ganesan & Vadivelu 2019;Miodonśki et al. 2019). Therefore, in full-scale applications of Anammox process, in case of a sudden toxicity, recovery would be a better way than restarting it. ...
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... However, most of the above-mentioned studies were based on the results of small-scale tests obtained from sequential batch experiments, and pilot tests or engineering application data for continuous water inflow have rarely been reported. Anammox bacteria are extremely sensitive to their living environment (Khramenkov et al., 2013;Miodoński et al., 2019;Strous et al., 1998). In pilot-scale and engineering applications, due to changes in the reactor and its operating conditions, relevant research results would likely differ somewhat, or even significantly, from those of small-scale tests. ...
Article
p>A pilot-scale sequencing batch reactor (SBR) for anaerobic ammonium oxidation (anammox) of bacteria culture was used along with a batch experimental reaction device to study the effect of NO2--N concentration on the activity of anammox bacteria and the recovery of N2H4 on anammox bacteria after inhibition by high concentrations of NO2--N. The optimal influent NO2--N concentration in the pilot-scale reactor was 72.0 mg/L, with its total nitrogen consumption being approximately 40.0 g/d. Influent water NO2--N concentrations greater than 100 mg/L had a serious inhibitory effect on the anammox bacteria. At an influent NO2--N concentration of 120.35 mg/L, the addition of 10.0-15.0 mg/L of N2H4, restored the activity of granular anammox bacteria; the total nitrogen consumption was increased by 69.96%. Microbiological analysis showed that a change in NO2--N concentration within the range of 18.87-115.39 mg/L did not affect the microbial population structure of the pilot-scale reactor, wherein Candidatus Kuenenia was the dominant bacterial species. In samples collected at stages A0 (sludge inoculation), A20 (the number indicates the NO2--N concentration, which, in this stage, was 20 mg/L), A40, A60, A80, and A100, the proportion of Candidatus Kuenenia was 27%, 23%, 36%, 26%, 34%, and 33%, respectively.</p
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Article
In this study, the start-up of anammox in a sequencing batch reactor (SBR) using conventional activated and anaerobic sludge in 1:1 ratio (v/v) as inoculum was achieved using an unconventional strategy. The ratio of NH4+-N to NO2−–N in the influent was not maintained as per the stoichiometry (1:1.32) of anammox and rather varied depending on the effluent characteristics. Nitrite was omitted during its accumulation period to avoid its toxicity during the start-up phase. The SBR having polyurethane foam impregnated with activated carbon (Levapor® carriers) was operated for 212 d (temperature, 37 °C; influent pH, 8). Anammox process was started up in ~95 d with 85% average total nitrogen (TN) removal. Thereafter, the reactor showed average TN removal efficiency of 85% and exhibited an average NH4+-N and NO2−–N removals of 99.9% each at maximum influent NH4+-N and NO2−–N concentrations of 200 mg L−1 and 264 mg L−1, respectively. The 16S rRNA gene amplicon sequencing analysis of suspended sludge samples (100 d, 150 d, and 186 d) from the reactor revealed the dominance of infrequently occurring anammox bacterial genus Candidatus Jettenia in the reactor. The phyla Chloroflexi, Proteobacteria, and Bacteriodetes were also detected in the reactor.
... The startup of Anammox process in reactors with different biomass carriers (sponge, volcanic rock and charcoal) showed no difference in the final nitrogen removal rate (NRR), however they were observed to have impacted the time needed to obtain certain NRR. Thus, its proper selection can influence the start-up time (Miodoński et al. 2019). Discussed below are some biomass carriers and their respective effects on the Anammox start-up and/or performance. ...
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