Determination of the energy, mass flow and temperature parameters in combustion systems of agricultural biomass residues

dc.contributor.buuauthorÜnal, Halil
dc.contributor.buuauthorKara, Ali
dc.contributor.departmentUludağ Üniversitesi/Ziraat Fakültesi/Biyosistem Mühendisliği Bölümü.tr_TR
dc.contributor.departmentUludağ Üniversitesi/Fen-Edebiyat Fakültesi/Kimya Bölümü.tr_TR
dc.contributor.orcid0000-0003-2457-6314tr_TR
dc.contributor.researcheridAAH-4410-2021tr_TR
dc.contributor.scopusid55807866400tr_TR
dc.contributor.scopusid7102824859tr_TR
dc.date.accessioned2023-08-15T07:13:36Z
dc.date.available2023-08-15T07:13:36Z
dc.date.issued2017-06-28
dc.description.abstractAim : This study was carried out to determine the energy, mass flow and temperature computations of agricultural biomass. Methodology : The feasibility of the technique which enable to formulate a balanced chemical equation using the parameters of biomass moisture content and excess air utilized in combustion was determined for agricultural biomass residues (corn cob and hazelnut shell). The chimney gas composition was calculated assuming that carbon dioxide and water were completely consumed. The combustion temperature was obtained with an energy balance. Results : Because of the error value of corn cob was negative, accepted combustion heat of this fuel was determined high (1400 degrees K) and concluded. It should have been reduced down to feasible value of this temperature. On the other hand, because of the error value for hazelnut shell was positive, raising the combustion heat is recommended. Feasible combustion heats for corn cob and hazelnut shell were 1389 degrees K and 1437 degrees K, respectively. While heat of combustion of corn cob in dry basis was 1436 degrees K for excess air parameter 1.0, the heat of combustion in 0.5 moisture level was 1132 degrees K with 27% reduction. The hazelnut shell combustion heat was also determined as 1205 degrees K with about 23% reduction. The net heats of combustion of corn cob and hazelnut shells in wet basis were determined as 13,109 and 15,775 kJ kg(-1), respectively. Interpretation : The biomass moisture, excess air and heat losses from system were in accordance with each other.en_US
dc.identifier.citationÜnal, H. ve Kara, A. (2017). ''Determination of the energy, mass flow and temperature parameters in combustion systems of agricultural biomass residues''. Journal of Environmental Biology, 38(5), Special Issue, 1085-1093.en_US
dc.identifier.endpage1093tr_TR
dc.identifier.issn0254-8704
dc.identifier.issue5, Special Issueen_US
dc.identifier.scopus2-s2.0-85030983818tr_TR
dc.identifier.startpage1085tr_TR
dc.identifier.urihttps://doi.org/10.22438/jeb/38/5(SI)/GM-27
dc.identifier.urihttps://www.cabdirect.org/cabdirect/abstract/20183173930
dc.identifier.urihttp://hdl.handle.net/11452/33492
dc.identifier.volume38tr_TR
dc.identifier.wos000413107700027tr_TR
dc.indexed.scopusScopusen_US
dc.indexed.wosSCIEen_US
dc.language.isoenen_US
dc.publisherTriveni Enterprisesen_US
dc.relation.journalJournal of Environmental Biologyen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergitr_TR
dc.rightsinfo:eu-repo/semantics/openAccessen_US
dc.subjectEnvironmental sciences & ecologyen_US
dc.subjectAgricultural residuesen_US
dc.subjectBiomassen_US
dc.subjectCombustion heaten_US
dc.subjectCorn coben_US
dc.subjectHazelnut shellen_US
dc.subjectCorylusen_US
dc.subjectZea maysen_US
dc.subjectBiomassen_US
dc.subjectCarbon dioxideen_US
dc.subjectCombustionen_US
dc.subjectCrop residueen_US
dc.subjectEnergy balanceen_US
dc.subjectEnergy flowen_US
dc.subjectFeasibility studyen_US
dc.subjectMass transferen_US
dc.subjectMoisture contenten_US
dc.subjectParameter estimationen_US
dc.subjectShellen_US
dc.subjectTemperature anomalyen_US
dc.subject.scopusFluidized Bed Combustors; Spontaneous Combustion; Gasificationen_US
dc.subject.wosEnvironmental sciencesen_US
dc.titleDetermination of the energy, mass flow and temperature parameters in combustion systems of agricultural biomass residuesen_US
dc.typeArticle
dc.wos.quartileQ4en_US

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