Experimental study of inverted annular film boiling in a vertical tube cooled by R-134a

► Heat transfer coefficient vs. quality curve can be divided into four regions depending on the flow regime. ► Film boiling heat transfer coefficient increases with increasing pressure and mass flux. ► Heat flux has weak effect on film boiling heat transfer coefficient. ► Inlet subcooling affects he...

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Published inInternational journal of multiphase flow Vol. 37; no. 1; pp. 67 - 75
Main Authors Nakla, Meamer El, Groeneveld, D.C., Cheng, S.C.
Format Journal Article
LanguageEnglish
Published Kidlington Elsevier Ltd 2011
Elsevier
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Summary:► Heat transfer coefficient vs. quality curve can be divided into four regions depending on the flow regime. ► Film boiling heat transfer coefficient increases with increasing pressure and mass flux. ► Heat flux has weak effect on film boiling heat transfer coefficient. ► Inlet subcooling affects heat transfer coefficient just downstream of CHF location. An experimental investigation of inverted annular film boiling heat transfer has been performed for vertical up-flow in a round tube. The experiments used R-134a coolant and covered a pressure range of 640–2390 kPa (water equivalent range: 4000–14,000 kPa) and a mass flux range of 500–4000 kg m −2 s −1 (water equivalent range: 700–5700 kg m −2 s −1). The inlet qualities of the tests ranged from −0.75 to −0.03. The hot-patch technique was used to obtain the subcooled film boiling measurements. It was found that the heat transfer vs. quality curve can be divided into four different regions, each characterized by a different mechanisms and trends. These regions are dependent on pressure, mass flux and local quality. A detailed examination of the parametric trends of the heat transfer coefficient with respect to mass flux, inlet quality, heat flux and pressure was performed; reasonably good agreement between observed trends and those reported in the literature were noted.
Bibliography:ObjectType-Article-2
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content type line 23
ISSN:0301-9322
1879-3533
DOI:10.1016/j.ijmultiphaseflow.2010.08.006