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http://hdl.handle.net/11452/33404
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DC Field | Value | Language |
---|---|---|
dc.contributor.author | Keskinler, Bülent | - |
dc.date.accessioned | 2023-08-08T11:40:21Z | - |
dc.date.available | 2023-08-08T11:40:21Z | - |
dc.date.issued | 2017-08 | - |
dc.identifier.citation | Şağban, F. O. T. vd. (2017). ''Hydrodynamic cavitation of waste activated sludge''. Environmental Engineering Science, 35(8), 775-784. | en_US |
dc.identifier.issn | 1557-9018 | - |
dc.identifier.uri | https://doi.org/10.1089/ees.2016.0408 | - |
dc.identifier.uri | https://www.liebertpub.com/doi/10.1089/ees.2016.0408 | - |
dc.identifier.uri | 1092-8758 | - |
dc.identifier.uri | http://hdl.handle.net/11452/33404 | - |
dc.description.abstract | Hydrodynamic cavitation systems have shown considerable promise for wastewater treatment. These systems are also used as a sludge pretreatment device to increase treatment efficiency of anaerobic sludge digestion systems. Although there are some literature related to disintegration of waste-activated sludge by hydrodynamic cavitation, effects of some operational variables in an orifice-based system, such as cavitation number and orifice diameter on sludge solubilization efficiency, are missing. In this study, waste-activated sludge that originated from a food processing facility was disintegrated mechanically on a laboratory scale using an orifice-based hydrodynamic cavitator. Use of NaOH, Ca(OH)(2), and H2O2 together with hydrodynamic cavitation was also evaluated. Results showed that after 150min of cavitation, disintegration degrees of 32% to 60% were obtained. Based on results, optimum cavitation number and orifice diameter selected for disintegration of waste-activated sludge were 0.2 and 3mm, respectively. Enhanced solubilization was achieved in the case of hydrodynamic cavitation combined with chemical addition. The best results for the disintegration of solids and organic carbon release in terms of soluble chemical oxygen demand (SCOD) were obtained for the combined system of H2O2 addition with a dose of 20mg/L and hydrodynamic cavitation. According to biochemical methane potential test (BMP) results, 20% to 89% higher biogas production was observed in disintegrated sludges comparing to raw sludge. | en_US |
dc.language.iso | en | en_US |
dc.publisher | Mary Ann Liebert | en_US |
dc.rights | info:eu-repo/semantics/closedAccess | en_US |
dc.subject | Engineering | en_US |
dc.subject | Environmental sciences & ecology | en_US |
dc.subject | Waste-activated sludge | en_US |
dc.subject | Cavitation number | en_US |
dc.subject | Sludge disintegration | en_US |
dc.subject | Hydrodynamic cavitation | en_US |
dc.subject | Orifice | en_US |
dc.subject | Advanced oxidation process | en_US |
dc.subject | Anaerobic-digestion | en_US |
dc.subject | Water treatment | en_US |
dc.subject | Ultrasonic pretreatment | en_US |
dc.subject | Combined alkaline | en_US |
dc.subject | Degradation | en_US |
dc.subject | Disintegration | en_US |
dc.subject | Solubilization | en_US |
dc.subject | Optimization | en_US |
dc.subject | Carbamazepine | en_US |
dc.subject | Anaerobic sludge digestion | en_US |
dc.subject | Biochemical methane potential | en_US |
dc.subject | Cavitation number | en_US |
dc.subject | Disintegration degrees | en_US |
dc.subject | Hydrodynamic cavitations | en_US |
dc.subject | Sludge disintegration | en_US |
dc.subject | Soluble chemical oxygen demands | en_US |
dc.subject | Waste activated sludges | en_US |
dc.subject | Sludge digestion | en_US |
dc.title | Hydrodynamic cavitation of waste activated sludge | en_US |
dc.type | Article | en_US |
dc.identifier.wos | 000417905200001 | tr_TR |
dc.identifier.scopus | 2-s2.0-85051468335 | tr_TR |
dc.relation.tubitak | 114Y523 | tr_TR |
dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi | tr_TR |
dc.contributor.department | Uludağ Üniversitesi/Mühendislik Fakültesi/Çevre Mühendisliği Bölümü. | tr_TR |
dc.contributor.orcid | 0000-0002-6364-4087 | tr_TR |
dc.identifier.startpage | 775 | tr_TR |
dc.identifier.endpage | 784 | tr_TR |
dc.identifier.volume | 35 | tr_TR |
dc.identifier.issue | 8 | tr_TR |
dc.relation.journal | Environmental Engineering Science | en_US |
dc.contributor.buuauthor | Şaǧban, Fatma Olcay Topaç | - |
dc.contributor.buuauthor | Dindar, Efsun | - |
dc.contributor.buuauthor | Çırakoğlu, Canan | - |
dc.contributor.researcherid | AAH-1853-2021 | tr_TR |
dc.contributor.researcherid | AAH-1131-2021 | tr_TR |
dc.relation.collaboration | Yurt içi | tr_TR |
dc.subject.wos | Engineering, environmental | en_US |
dc.subject.wos | Environmental sciences | en_US |
dc.indexed.wos | SCIE | en_US |
dc.indexed.scopus | Scopus | en_US |
dc.wos.quartile | Q3 | en_US |
dc.contributor.scopusid | 16319975800 | tr_TR |
dc.contributor.scopusid | 23984709100 | tr_TR |
dc.contributor.scopusid | 57203389417 | tr_TR |
dc.subject.scopus | Cavitation; Advanced Oxidation; Ultrasound | en_US |
dc.subject.emtree | Biogas | en_US |
dc.subject.emtree | Organic carbon | en_US |
dc.subject.emtree | Activated sludge | en_US |
dc.subject.emtree | Anaerobic digestion | en_US |
dc.subject.emtree | Article | en_US |
dc.subject.emtree | Biodegradability | en_US |
dc.subject.emtree | Biofuel production | en_US |
dc.subject.emtree | Chemical oxygen demand | en_US |
dc.subject.emtree | Decomposition | en_US |
dc.subject.emtree | Energy consumption | en_US |
dc.subject.emtree | Flow rate | en_US |
dc.subject.emtree | Food processing | en_US |
dc.subject.emtree | Hydrodynamics | en_US |
dc.subject.emtree | Ozonation | en_US |
dc.subject.emtree | Sludge digestion | en_US |
dc.subject.emtree | Solubilization | en_US |
dc.subject.emtree | pH | en_US |
dc.subject.emtree | Waste water management | en_US |
Appears in Collections: | Scopus Web of Science |
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