Publication: Anammox-zeolite system acting as buffer to achieve stable effluent nitrogen values
| dc.contributor.author | MERTOĞLU, BÜLENT | |
| dc.contributor.author | KALKAN AKTAN, ÇİĞDEM | |
| dc.contributor.author | BAKIRCI, KOZET | |
| dc.contributor.authors | Yapsakli, Kozet; Aktan, Cigdem Kalkan; Mertoglu, Bulent | |
| dc.date.accessioned | 2022-03-12T20:30:46Z | |
| dc.date.accessioned | 2026-01-11T08:27:52Z | |
| dc.date.available | 2022-03-12T20:30:46Z | |
| dc.date.issued | 2017 | |
| dc.description.abstract | For a successful nitrogen removal, Anammox process needs to be established in line with a stable partial nitritation pretreatment unit since wastewater influent is mostly unsuitable for direct treatment by Anammox. Partial nitritation is, however, a critical bottleneck for the nitrogen removal since it is often difficult to maintain the right proportions of NO2-N and NH4-N during long periods of time for Anammox process. This study investigated the potential of Anammox-zeolite biofilter to buffer inequalities in nitrite and ammonium nitrogen in the influent feed. Anammox-zeolite biofilter combines the ion-exchange property of zeolite with the biological removal by Anammox process. Continuous-flow biofilter was operated for 570 days to test the response of Anammox-zeolite system for irregular ammonium and nitrite nitrogen entries. The reactor demonstrated stable and high nitrogen removal efficiencies (approximately 95 %) even when the influent NO2-N to NH4-N ratios were far from the stoichiometric ratio for Anammox reaction (i.e. NO2-N to NH4-N ranging from 0 to infinity). This is achieved by the sorption of surplus NH4-N by zeolite particles in case ammonium rich influent came in excess with respect to Anammox stoichiometry. Similarly, when ammonium-poor influent is fed to the reactor, ammonium desorption took place due to shifts in ion-exchange equilibrium and deficient amount were supplied by previously sorbed NH4-N. Here, zeolite acted as a preserving reservoir of ammonium where both sorption and desorption took place when needed and this caused the Anammox-zeolite system to act as a buffer system to generate a stable effluent. | |
| dc.identifier.doi | 10.1007/s10532-016-9778-1 | |
| dc.identifier.eissn | 1572-9729 | |
| dc.identifier.issn | 0923-9820 | |
| dc.identifier.pubmed | 27807679 | |
| dc.identifier.uri | https://hdl.handle.net/11424/234208 | |
| dc.identifier.wos | WOS:000394181500006 | |
| dc.language.iso | eng | |
| dc.publisher | SPRINGER | |
| dc.relation.ispartof | BIODEGRADATION | |
| dc.rights | info:eu-repo/semantics/closedAccess | |
| dc.subject | Anammox | |
| dc.subject | Biodegradation | |
| dc.subject | Zeolite | |
| dc.subject | Ion-exchange | |
| dc.subject | Ammonium removal | |
| dc.subject | ION-EXCHANGE | |
| dc.subject | AMMONIUM OXIDATION | |
| dc.subject | BIOLOGICAL REGENERATION | |
| dc.subject | GRANULAR SLUDGE | |
| dc.subject | FLUIDIZED-BED | |
| dc.subject | WASTE-WATER | |
| dc.subject | REMOVAL | |
| dc.subject | NITRIFICATION | |
| dc.subject | REACTOR | |
| dc.subject | CLINOPTILOLITE | |
| dc.title | Anammox-zeolite system acting as buffer to achieve stable effluent nitrogen values | |
| dc.type | article | |
| dspace.entity.type | Publication | |
| oaire.citation.endPage | 79 | |
| oaire.citation.issue | 1 | |
| oaire.citation.startPage | 69 | |
| oaire.citation.title | BIODEGRADATION | |
| oaire.citation.volume | 28 |
