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Document IIF

Etude expérimentale de l'ébullition de n-pentane à travers un faisceau de tubes horizontal : écoulement diphasique et caractéristiques de transfert de chaleur.

Experimental investigations on boiling of n-pentane across a horizontal tube bundle: two-phase flow and heat transfer characteristics.

Auteurs : ROSER R., THONON B., MERCIER P.

Type d'article : Article, Article de la RIF

Résumé

This paper presents the heat transfer characteristics obtained from an experimental investigation on flow boiling of n-pentane across a horizontal tube bundle. The tubes are plain with an outside diameter of 19.05 millimeters and the bundle arrangement is inverse staggered with a pitch to diameter ratio of 1.33. The test conditions consist of reduced pressure between 0.006 and 0.015, mass velocity from 14 to 44 kg/m2s, heat flux up to 60 kW/m2 and vapour quality up to 60%. The convective evaporation is found to have a significant effect on the heat transfer coefficient, coexisting with nucleate boiling. An asymptotic model allows the prediction of the heat transfer data with a fitted value of n=1.5. A strong mass velocity effect is observed for the enhancement factor, implying that the correlations available from the literature for the convective evaporation will fail in predicting the present data. This effect decreases as the mass velocity increases.

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Format PDF

Pages : 536-547

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Détails

  • Titre original : Experimental investigations on boiling of n-pentane across a horizontal tube bundle: two-phase flow and heat transfer characteristics.
  • Identifiant de la fiche : 2000-0133
  • Langues : Anglais
  • Source : International Journal of Refrigeration - Revue Internationale du Froid - vol. 22 - n. 7
  • Date d'édition : 11/1999

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