Analysis of low-grade heat driven ethanol-silica gel adsorption chiller

dc.authoridDemir, Hasan/0000-0002-9278-9648
dc.authoridGediz Ilis, Gamze/0000-0001-8366-5427
dc.authorscopusid57329590000
dc.authorscopusid57223035605
dc.authorscopusid57192707075
dc.authorscopusid6603833743
dc.authorwosidDemir, Hasan/B-6603-2012
dc.contributor.authorHabash, Rami
dc.contributor.authorIlis, Gamze Gediz
dc.contributor.authorDemir, Hasan
dc.contributor.authorOztop, Hakan Fehmi
dc.date.accessioned2024-05-25T11:26:44Z
dc.date.available2024-05-25T11:26:44Z
dc.date.issued2021
dc.departmentOkan Universityen_US
dc.department-temp[Habash, Rami] Istanbul Okan Univ, Mechatron Engn Dept, Istanbul, Turkey; [Ilis, Gamze Gediz] Gebze Tech Univ, Mech Engn Dept, Gebze, Turkey; [Demir, Hasan] Osmaniye Korkut Ata Univ, Chem Engn Dept, Osmaniye, Turkey; [Oztop, Hakan Fehmi] Firat Univ, Technol Fac, Dept Mech Engn, Elazig, Turkeyen_US
dc.descriptionDemir, Hasan/0000-0002-9278-9648; Gediz Ilis, Gamze/0000-0001-8366-5427en_US
dc.description.abstractThe main objective of this study is to design a low-grade heat driven ethanol-silica gel adsorption chiller. The low-grade waste heat is utilized in an adsorption chiller. For this purpose, an innovative bed heat exchanger including a condenser embedded inside the adsorbent bed is uniquely designed. The silica gel/ethanol pair is examined both analytically and numerically in this article. The cycles of the adsorption chiller are performed experimentally. The obtained isotherm for the silica gel/ethanol fitted to Type III isotherm behavior. The obtained equations of isotherm are also validated numerically. The new adsorption chiller design used in this study has reduced the desorption temperature for silica gel/ethanol pair to 37 degrees C which will widen the application area of adsorption chillers. The COMSOL Multiphysics program is used for 2-D numerical analysis of adsorbent bed. The mass transfer inside of the particle, the heat transfer in porous media, and Darcy law are used for analyzing the heat and mass transfer of the bed. Temperature and concentration distributions of adsorbent bed during the duration of adsorption and desorption processes are examined numerically. The specific cooling power and volumetric cooling power values of the system are found as 20.2 Wkg1 and 4.5 kWm 3, respectively.en_US
dc.identifier.citation9
dc.identifier.doi10.1016/j.tsep.2021.101125
dc.identifier.issn2451-9049
dc.identifier.scopus2-s2.0-85118842210
dc.identifier.scopusqualityQ1
dc.identifier.urihttps://doi.org/10.1016/j.tsep.2021.101125
dc.identifier.urihttps://hdl.handle.net/20.500.14517/1013
dc.identifier.volume26en_US
dc.identifier.wosWOS:000730121300003
dc.identifier.wosqualityQ1
dc.language.isoen
dc.publisherElsevieren_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectLow-grade heat sourceen_US
dc.subjectSilica gelen_US
dc.subjectethanol pairen_US
dc.subjectAdsorption chilleren_US
dc.subjectCombined condenser-bed designen_US
dc.titleAnalysis of low-grade heat driven ethanol-silica gel adsorption chilleren_US
dc.typeArticleen_US
dspace.entity.typePublication

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