The effect of input temperatures on the absorber parameters

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dc.contributor.buuauthorAtmaca, İbrahim
dc.contributor.buuauthorAltuğ, Yiğit
dc.contributor.buuauthorKılıç, Muhsin
dc.contributor.departmentUludağ Üniversitesi/Mühendislik Fakültesi/Makina Mühendisliği Bölümü.tr_TR
dc.contributor.orcid0000-0003-2113-4510tr_TR
dc.contributor.researcheridC-4999-2016tr_TR
dc.contributor.researcheridO-2253-2015tr_TR
dc.contributor.scopusid7801455908tr_TR
dc.contributor.scopusid7006225124tr_TR
dc.contributor.scopusid57202677637tr_TR
dc.date.accessioned2021-10-23T12:38:24Z
dc.date.available2021-10-23T12:38:24Z
dc.date.issued2002-11
dc.description.abstractIn an absorption cooling system, simultaneous heat and mass transfer operations take place in the absorber and generator. The performance of an absorber is of paramount importance on the coefficient of performance and the manufacturing cost of an absorption machine. Increasing heat and mass transfer coefficients in an absorber decreases the heat transfer area of the absorber, as a result of this the cost of the system can be reduced. The absorption of water vapor in aqueous solutions of lithium bromide is modelled for a falling-film, vertical-tube absorber. Heat and mass transfer coefficients are determined by calculating temperature and concentration variations at the falling film in the absorber. Then mean Nusselt and Sherwood numbers are determined to see the changes in the heat and mass transfer. Subsequently, a modular computer program has been developed for absorption systems to simulate various cycle configurations and absorber parameters. So, the effect of hot water, chilled water and cooling water inlet temperatures on the coefficients of performance, Nusselt and Sherwood numbers and the surface area of the absorber are studied with the simulation program. The results can be used to optimise the commercial absorption chillers.en_US
dc.identifier.citationAtmaca, İ. vd. (2002). "The effect of input temperatures on the absorber parameters". International Communications in Heat And Mass Transfer, 29(8), 1177-1186.en_US
dc.identifier.endpage1186tr_TR
dc.identifier.issn0735-1933
dc.identifier.issue8tr_TR
dc.identifier.scopus2-s2.0-0036873434tr_TR
dc.identifier.startpage1177tr_TR
dc.identifier.urihttps://doi.org/I10.1016/S0735-1933(02)00446-3
dc.identifier.urihttps://www.sciencedirect.com/science/article/pii/S0735193302004463
dc.identifier.urihttp://hdl.handle.net/11452/22456
dc.identifier.volume29tr_TR
dc.identifier.wos000179870700017tr_TR
dc.indexed.scopusScopusen_US
dc.indexed.wosSCIEen_US
dc.language.isoenen_US
dc.publisherPergamon-Elsevier Scienceen_US
dc.relation.journalInternational Communications in Heat And Mass Transferen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergitr_TR
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectMass-transferen_US
dc.subjectAbsorptionen_US
dc.subjectHeaten_US
dc.subjectThermodynamicsen_US
dc.subjectMechanicsen_US
dc.subjectTemperature effecten_US
dc.subjectMass transferen_US
dc.subjectCooling systemsen_US
dc.subjectAbsorption chillersen_US
dc.subjectAbsorptionen_US
dc.subjectComputer programmingen_US
dc.subjectHeat transferen_US
dc.subjectLithium compoundsen_US
dc.subjectNusselt numberen_US
dc.subjectThermal effectsen_US
dc.subjectVaporsen_US
dc.subjectWateren_US
dc.subject.scopusAbsorption Refrigeration; Solar Cooling; Lithium Bromideen_US
dc.subject.wosThermodynamicsen_US
dc.subject.wosMechanicsen_US
dc.titleThe effect of input temperatures on the absorber parametersen_US
dc.typeArticle
dc.wos.quartileQ4en_US

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