Bu öğeden alıntı yapmak, öğeye bağlanmak için bu tanımlayıcıyı kullanınız:
http://hdl.handle.net/11452/31350
Tüm üstveri kaydı
Dublin Core Alanı | Değer | Dil |
---|---|---|
dc.contributor.author | Lütfi, Akça | - |
dc.contributor.author | Hürrem, Bayhan | - |
dc.date.accessioned | 2023-03-06T07:04:54Z | - |
dc.date.available | 2023-03-06T07:04:54Z | - |
dc.date.issued | 2003 | - |
dc.identifier.citation | Nalbur, B. E. vd. (2003). “Nitrogen removal during secondary treatment by aquatic systems”. Water Science and Technology, 48(11-12), 355-361. | en_US |
dc.identifier.issn | 0273-1223 | - |
dc.identifier.uri | http://hdl.handle.net/11452/31350 | - |
dc.description | Bu çalışma, 24-26 Eylül 2002 tarihleri arasında İstanbul[Türkiye]’de düzenlenen 5. International Conference on Small Water and Wastewater Treatment Systems'de bildiri olarak sunulmuştur. | tr_TR |
dc.description.abstract | Within the context of this study, two lab-scale aquatic plant reactors consisting of duckweed (Lemna minor) ponds, were investigated for the removal of nitrogen forms during the secondary treatment of domestic wastewater. TKN, NH3-N and NO3-N parameters have been measured in both reactors for hydraulic retention times ranging from 3.3 days to 23 days and at various distances from the inlet of reactors. The results were evaluated for hydraulic retention times, hydraulic loading rates and mass loading rates. It was concluded that hydraulic and mass loading parameters were more meaningful than hydraulic retention time. Optimum nitrogen removal values of hydraulic loading rate and mass loading rate were found to be 1.2 cm/day and 90-160 mg TKN/m(2)-day, respectively. At the higher and lower loading rates, nitrogen removal efficiency was lower than those at optimum conditions. Effluent TKN concentration was around 2.5 to 3.0 mg/l while NH3-N concentration was almost zero at these loading conditions. On the other hand, effluent NO3-N concentrations changed between 7 mg/l to 11 mg/l. When investigating the longitudinal profile, values were reduced rapidly along the reactors. It was concluded that most of the nitrogen conversion occurred at the beginning of the reactor. | en_US |
dc.language.iso | en | en_US |
dc.publisher | IWA Publishing | en_US |
dc.rights | info:eu-repo/semantics/closedAccess | en_US |
dc.subject | Aquatic ponds | en_US |
dc.subject | Duckweed | en_US |
dc.subject | Nitrogen removal | en_US |
dc.subject | Water treatment systems | en_US |
dc.subject | Engineering | en_US |
dc.subject | Environmental sciences and ecology | en_US |
dc.subject | Water resources | en_US |
dc.subject | Lemna | en_US |
dc.subject | Lemna minor | en_US |
dc.subject | Bioreactors | en_US |
dc.subject | Nitrogen compounds | en_US |
dc.subject | Surface waters | en_US |
dc.subject | Wastewater | en_US |
dc.subject | Aquatic plant reactors | en_US |
dc.title | Nitrogen removal during secondary treatment by aquatic systems | en_US |
dc.type | Article | en_US |
dc.type | Proceedings Paper | en_US |
dc.identifier.wos | 000188094900046 | tr_TR |
dc.identifier.scopus | 2-s2.0-0346008004 | tr_TR |
dc.relation.publicationcategory | Konferans Öğesi - Uluslararası | tr_TR |
dc.contributor.department | Uludağ Üniversitesi/Mühendislik Fakültesi/Çevre Mühendisliği Bölümü. | tr_TR |
dc.identifier.startpage | 355 | tr_TR |
dc.identifier.endpage | 361 | tr_TR |
dc.identifier.volume | 48 | tr_TR |
dc.identifier.issue | 11-12 | tr_TR |
dc.relation.journal | Water Science and Technology | en_US |
dc.contributor.buuauthor | Berrak, Erol Nalbur | - |
dc.contributor.researcherid | AAG-8493-2021 | tr_TR |
dc.relation.collaboration | Yurt içi | tr_TR |
dc.identifier.pubmed | 14753556 | tr_TR |
dc.subject.wos | Engineering, environmental | en_US |
dc.subject.wos | Environmental sciences | en_US |
dc.subject.wos | Water resources | en_US |
dc.indexed.wos | SCIE | en_US |
dc.indexed.wos | CPCIS | en_US |
dc.indexed.scopus | Scopus | en_US |
dc.indexed.pubmed | PubMed | en_US |
dc.wos.quartile | Q3 (Environmental sciences) | en_US |
dc.wos.quartile | Q2 | en_US |
dc.contributor.scopusid | 8127615900 | tr_TR |
dc.subject.scopus | Araceae; Bioremediation; Landoltia Punctata | en_US |
dc.subject.emtree | Aquatic environment | en_US |
dc.subject.emtree | Concentration (parameters) | en_US |
dc.subject.emtree | Conference paper | en_US |
dc.subject.emtree | Controlled study | en_US |
dc.subject.emtree | Domestic waste | en_US |
dc.subject.emtree | Effluent | en_US |
dc.subject.emtree | Hydraulic permeability | en_US |
dc.subject.emtree | Measurement | en_US |
dc.subject.emtree | Nutrient | en_US |
dc.subject.emtree | Pond | en_US |
dc.subject.emtree | Reactor | en_US |
dc.subject.emtree | Waste component removal | en_US |
dc.subject.emtree | Waste water management | en_US |
dc.subject.emtree | Waste water treatment plant | en_US |
dc.subject.emtree | Ammonia | en_US |
dc.subject.emtree | Nitrate | en_US |
dc.subject.emtree | Nitrogen | en_US |
Koleksiyonlarda Görünür: | Scopus Web of Science |
Bu öğenin dosyaları:
Bu öğeyle ilişkili dosya bulunmamaktadır.
DSpace'deki bütün öğeler, aksi belirtilmedikçe, tüm hakları saklı tutulmak şartıyla telif hakkı ile korunmaktadır.