完整後設資料紀錄
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dc.contributor.authorLee, Bing-Hungen_US
dc.contributor.authorSian, Rony A.en_US
dc.contributor.authorWang, Chi-Chuanen_US
dc.date.accessioned2019-06-03T01:08:34Z-
dc.date.available2019-06-03T01:08:34Z-
dc.date.issued2019-04-26en_US
dc.identifier.issn0737-3937en_US
dc.identifier.urihttp://dx.doi.org/10.1080/07373937.2018.1454940en_US
dc.identifier.urihttp://hdl.handle.net/11536/151937-
dc.description.abstractThe present study proposes a rationally based heat pump clothes dryer model which is capable of handling transient behaviors of both air-side and refrigerant side. The model can take into account the geometrical variation of the heat exchangers. Yet the proposed model is free from extra constraints that were normally imposed by previous studies. The simulation shows that there exist three stages in a typical drying process, including a preheat stage, followed by a constant evaporation stage, and finally a falling drying rate period. The calculation indicates that the variation of the clothes temperature and the system suction/discharge pressure show an appreciable rise in the first stage, remain nearly unchanged at the second stage, and increase again at the final stage of drying process. Also, the corresponding maximum specific moisture extraction rate (SMER) peaks at the end of the second stage while the corresponding coefficient of performance (COP) drops continuously. The simulation also indicates that increasing the air volumetric flowrate yields a lower discharge/suction pressure, a higher COP value, and a shorter drying time. The results also suggested that a good strategy to maximize COP is initiated by a low volumetric rate during the preheat stage, increasing it during the second stage and lowering it to an intermediate flowrate at the end of the drying period. Increasing heat exchanger size, either by increasing heat exchanger width or the number of tube row, results in a lower suction/discharge pressure and a shorter drying time. Although both approaches adopt larger surface area to promote overall performance, it is found that increasing the width of heat exchanger yields more effective results.en_US
dc.language.isoen_USen_US
dc.subjectHeat pump dryingen_US
dc.subjectheat and mass transferen_US
dc.subjectmathematical modelingen_US
dc.titleA rationally based model applicable for heat pump tumble dryeren_US
dc.typeArticleen_US
dc.identifier.doi10.1080/07373937.2018.1454940en_US
dc.identifier.journalDRYING TECHNOLOGYen_US
dc.citation.volume37en_US
dc.citation.issue6en_US
dc.citation.spage691en_US
dc.citation.epage706en_US
dc.contributor.department機械工程學系zh_TW
dc.contributor.departmentDepartment of Mechanical Engineeringen_US
dc.identifier.wosnumberWOS:000466414900003en_US
dc.citation.woscount0en_US
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