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Combination of upflow anaerobic sludge blanket (UASB) reactor and partial nitritation/anammox moving bed biofilm reactor (MBBR) for municipal wastewater treatment
KTH, Skolan för arkitektur och samhällsbyggnad (ABE), Hållbar utveckling, miljövetenskap och teknik, Mark- och vattenteknik.
KTH, Skolan för arkitektur och samhällsbyggnad (ABE), Hållbar utveckling, miljövetenskap och teknik, Mark- och vattenteknik.
KTH, Skolan för arkitektur och samhällsbyggnad (ABE), Hållbar utveckling, miljövetenskap och teknik, Mark- och vattenteknik.
KTH, Skolan för arkitektur och samhällsbyggnad (ABE), Hållbar utveckling, miljövetenskap och teknik, Mark- och vattenteknik.
2015 (Engelska)Ingår i: Bioresource Technology, ISSN 0960-8524, E-ISSN 1873-2976, Vol. 180, s. 144-153Artikel i tidskrift (Refereegranskat) Published
Abstract [en]

In this study the combination of an upflow anaerobic sludge blanket (UASB) reactor and a deammonification moving bed biofilm reactor (MBBR) for mainstream wastewater treatment was tested. The competition between aerobic ammonium oxidizing bacteria (AOB) and nitrite oxidizing bacteria (NOB) was studied during a 5 months period of transition from reject water to mainstream wastewater followed by a 16 months period of mainstream wastewater treatment. The decrease of influent ammonium concentration led to a wash-out of suspended biomass which had a major contribution to nitrite production. Influence of a dissolved oxygen concentration and a transient anoxia mechanism of NOB suppression were studied. It was shown that anoxic phase duration has no effect on NOB metabolism recovery and oxygen diffusion rather than affinities of AOB and NOB to oxygen determine the rate of nitrogen conversion in a biofilm system. Anammox activity remained on the level comparable to reject water treatment systems.

Ort, förlag, år, upplaga, sidor
2015. Vol. 180, s. 144-153
Nyckelord [en]
Anammox, Mainstream deammonification, AOB, NOB, MBBR
Nationell ämneskategori
Naturresursteknik
Identifikatorer
URN: urn:nbn:se:kth:diva-161949DOI: 10.1016/j.biortech.2014.12.101ISI: 000349715700020PubMedID: 25600011Scopus ID: 2-s2.0-84921419582OAI: oai:DiVA.org:kth-161949DiVA, id: diva2:801035
Forskningsfinansiär
VINNOVASvenska institutet
Anmärkning

QC 20150408

Tillgänglig från: 2015-04-08 Skapad: 2015-03-20 Senast uppdaterad: 2017-12-04Bibliografiskt granskad
Ingår i avhandling
1. Anammox-based systems for nitrogen removal from mainstream municipal wastewater
Öppna denna publikation i ny flik eller fönster >>Anammox-based systems for nitrogen removal from mainstream municipal wastewater
2017 (Engelska)Doktorsavhandling, sammanläggning (Övrigt vetenskapligt)
Abstract [en]

Nitrogen removal from municipal wastewater with the application of deammonification process offers an operational cost reduction, especially if it is combined with a maximal use of organic content of wastewater for biogas production. In this thesis, two approaches for integration of the deammonification process into the municipal wastewater treatment scheme were studied.

The first approach is based on ammonium concentration from municipal wastewater by ion exchange followed by biological removal of ammonium from the concentrated stream by deammonification process. Experiments with synthetic and real municipal wastewater showed that strong acid cation resin is suitable for ammonium concentration due to its high exchange capacity and fast regeneration. Since NaCl was used for regeneration of ion exchange materials, spent regenerant had elevated salinity. The deammonification biomass was adapted to NaCl content of 10-15 g/L by step-wise salinity increase. The technology was tested in batch mode with 99.9 % of ammonium removal from wastewater with ion exchange and up to 95 % of nitrogen removal from spent regenerant by deammonification process.

The second studied approach was to apply anammox process to low-concentrated municipal wastewater in a moving bed biofilm reactor (MBBR) and integrated fixed film activated sludge (IFAS) system without a pre-concentration step. After a 5 months period of transition to mainstream wastewater the pilot plant was operated during 22 months and stable performance of one-stage deammonification was proven. Clear advantage of IFAS system was shown. The highest stable nitrogen removal efficiency of 70 % and a nitrogen removal rate of 55 g N/(m3·d) was reached. Moreover, the influence of operation conditions on competition between ammonium oxidizing bacteria (AOB) and nitrite oxidizing bacteria (NOB) was studied by literature review, batch tests and continuous pilot plant operation.

Ort, förlag, år, upplaga, sidor
KTH Royal Institute of Technology, 2017. s. 53
Serie
TRITA-LWR. PHD, ISSN 1650-8602 ; 2017:01
Nyckelord
Wastewater, Nitrogen removal, Ion exchange, Deammonification, Anammox, Mainstream
Nationell ämneskategori
Vattenbehandling
Forskningsämne
Mark- och vattenteknik
Identifikatorer
urn:nbn:se:kth:diva-202960 (URN)978-91-7729-317-0 (ISBN)
Disputation
2017-04-06, F3, Lindstedtsvägen 26, Stockholm, 09:30 (Engelska)
Opponent
Handledare
Anmärkning

QC 20170309

Tillgänglig från: 2017-03-09 Skapad: 2017-03-08 Senast uppdaterad: 2017-03-09Bibliografiskt granskad

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