Startup of pilot-scale single-stage nitrogen removal using anammox and partial nitritation (SNAP) reactor for waste brine treatment using marine anammox bacteria

https://doi.org/10.1016/j.jbiosc.2021.06.013Get rights and content

Highlights

  • Pilot scale SNAP reactor to treat waste brine was successfully started up for the first time.

  • Marine anammox bacteria affiliated to Candidatus Scalindua was enriched.

  • AOB granule formed precedingly provided favorable growth condition for anammox bacteria and worked as biomass carrier.

  • Application of mesh-screen contributed to the retention of SNAP sludge in the reactor.

This study is the first to demonstrate the startup of a pilot-scale single-stage nitrogen removal using anammox and partial nitritation (SNAP) reactor utilizing marine anammox bacteria. A complete mixing type reactor, continuously fed with waste brine obtained from a natural gas plant (salinity 3%, NH4+-N 130–180 mg/L) and having an effective volume of 2 m3, achieved stable operation at temperatures of 20–30°C with a maximum nitrogen removal rate of 1.43 kg-N/m3/day. During the startup process, along with a small amount of seed sludge, granular sludge was additionally inoculated as a biomass carrier for the enrichment of ammonia oxidizing bacteria (AOB), followed by the enrichment of anammox bacteria. A mesh screen equipped at the outlet of the reactor facilitated the successful sludge retention in the reactor. Analysis of bacterial community composition indicated that Candidatus Scalindua was successfully enriched in the pilot SNAP reactor. These methods for stable sludge retention in the reactor greatly contributed to the startup of the first pilot-scale SNAP reactor using marine anammox bacteria.

Section snippets

SNAP reactor

To investigate the startup method of the pilot-scale SNAP process for waste brine treatment, we used a complete mixing type reactor including settling zone with length, width, height, and working volume of 1.0 m, 1.0 m, 2.2 m, and 2 m3, respectively (Fig. 1). Waste brine (Table 1), generated from a natural gas plant, was supplied to the reactor at flow rates of 30–900 L/h. The trace element solution (30–200 mL) was added to the reactor three times per week. The trace element solution contained

Cultivation of AOB (phase 1 to 2)

After day 90 in phase 1, the bulky and fluffy sludge was enriched and the nitrification rate (NR) increased to 0.26 kg-N/m3/day on day 142 (Fig. 2A and B). However, the sludge was washed out because of its poor settleability. After the addition of freshwater anammox granules as a biomass carrier of AOB on day 477 in phase 2, NR sharply increased and reached to 0.77 kg-N/m3/day on day 493. DO concentration decreased from 5.0 mg/L in phase 1 to 0.5 mg/L in phase 2.

Cultivation of anammox bacteria (phase 3 to 4)

After the addition of anammox

Preceding AOB cultivation for anammox growth

In this study, AOB cultivation preceding anammox bacteria cultivation decreased the DO concentration to 0.5 mg/L and increased the nitrite production rate, which are favorable for the growth of anammox bacteria. DO inhibits the activity of anammox bacteria, while it is essential for the partial nitritation by AOB. Several studies have reported the inhibiting DO concentration of 5.0 mg/L for granular anammox sludge (31) and 0.5 mg/L for floc anammox sludge (32). Previous studies investigated the

Acknowledgments

This research was supported by the Keiyo Natural Gas Association.

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