Publication:
Optimization of the solar brine evaporation process: Introduction of a solar air heater

dc.contributor.authorPoblete, Rodrigo
dc.contributor.authorSalihoğlu, Nezih Kamil
dc.contributor.authorSalihoğlu, Güray
dc.contributor.buuauthorSALİHOĞLU, NEZİH KAMİL
dc.contributor.buuauthorSALİHOĞLU, GÜRAY
dc.contributor.departmentBursa Uludağ Üniversitesi/Mühendislik Fakültesi/Çevre Mühendisliği Bölümü.
dc.contributor.orcid0000-0002-7730-776X
dc.contributor.orcid0000-0003-0714-048X
dc.contributor.researcheridAAG-9399-2021
dc.contributor.researcheridAAG-9413-2021
dc.date.accessioned2024-07-11T11:40:05Z
dc.date.available2024-07-11T11:40:05Z
dc.date.issued2019-05-01
dc.description.abstractThe purpose of this study was to investigate the evaporation process of reject brine by using a solar system. The solar system contained a solar still coupled with a solar air heater (SAH). Solar still had a heated base, which was connected to the solar collector with a copper pipe. The influence of the introduction of the SAH to the system and increased levels of air mass flowrates was investigated. Variations in temperature and solar irradiation were monitored as well as brine evaporation. Introducing the SAH and increasing the air mass flowrate resulted in faster brine evaporation, higher utilization rate of solar radiation, higher brine, and base temperature levels within the solar still compared to the system without the SAH. The mean base temperature of the system with the SAH was 43.46 +/- 11.3 degrees C, while that of the system without the SAH was 30.62 +/- 7.35 degrees C. The use of the SAH and high air mass flowrates influenced the temperature distribution within the solar still, which affected the evaporation of the brine in a positive way. Introduction of the SAH and high air mass flowrate increased the drying efficiency of the solar system at a level of 120%. (c) 2018 American Institute of Chemical Engineers Environ Prog, 38:e13062, 2019
dc.identifier.doi10.1002/ep.13062
dc.identifier.issn1944-7442
dc.identifier.issue3
dc.identifier.urihttps://doi.org/10.1002/ep.13062
dc.identifier.urihttps://hdl.handle.net/11452/43200
dc.identifier.urihttps://aiche.onlinelibrary.wiley.com/doi/10.1002/ep.13062
dc.identifier.volume38
dc.identifier.wos000469045900034
dc.indexed.wosWOS.SCI
dc.language.isoen
dc.publisherWiley
dc.relation.journalEnvironmental Progress & Sustainable Energy
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.subjectPerformance evaluation
dc.subjectDesalination plant
dc.subjectThermal performance
dc.subjectSalt recovery
dc.subjectEnergy
dc.subjectSystem
dc.subjectDryer
dc.subjectDischarge
dc.subjectImpacts
dc.subjectDesign
dc.subjectAir mass flowrate
dc.subjectDrying efficiency
dc.subjectSolar air heater
dc.subjectSolar still
dc.subjectTemperature distribution
dc.subjectScience & technology - other topics
dc.subjectEngineering
dc.subjectEnvironmental sciences & ecology
dc.titleOptimization of the solar brine evaporation process: Introduction of a solar air heater
dc.typeArticle
dspace.entity.typePublication
relation.isAuthorOfPublication0eb38050-d0fe-4aa8-8ed9-ab965ef7a451
relation.isAuthorOfPublication76512d6e-0f48-4fcd-bf31-5be60d0790f7
relation.isAuthorOfPublication.latestForDiscovery0eb38050-d0fe-4aa8-8ed9-ab965ef7a451

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