A void fraction model for annular flow in horizontal tubes
β Scribed by Todd M. Harms; Daqing Li; Eckhard A. Groll; James E. Braun
- Publisher
- Elsevier Science
- Year
- 2003
- Tongue
- English
- Weight
- 172 KB
- Volume
- 46
- Category
- Article
- ISSN
- 0017-9310
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β¦ Synopsis
An important feature of detailed system simulation models for unitary air conditioners is the calculation of charge inventory. Void fraction determination in the two-phase regions of the heat exchangers is the primary challenge associated with charge inventory calculations. Annular flow is one of the predominant flow regimes encountered in horizontal heat exchangers. Analytical annular flow models typically fail to accurately represent void fraction. Thus, many of the available void fraction models are empirically based. To improve the prediction capabilities of void fraction models, a mechanistic void fraction model has been developed for annular flow in horizontal tubes. The present model considers the effect of momentum eddy diffusivity damping at the liquid-vapor interface. Two approaches are presented for determining the wall shear stress. The modeling results are compared to predictions from various void fraction models found in the literature. The present model is found to work well at moderate mass fluxes.
π SIMILAR VOLUMES
The pressure drop and void fraction of two-phase helium in a horizontal flow loop driven by a single stroke bellows pump at mass flow rates ranging from 0.5 to 2.0 g s-' and under system pressures between 0.65 and 1.2 atm are reported. The slip ratio (the ratio of the velocity of the gaseous phase o
A model has been developed to predict average void-fractions in horizontal and vertical two-phase flow based on a single flow parameter K and the slip velocity. The model is based on the assumptions that the radial distributions of liquid velocity and void-fraction can be represented by parabolic-ty
published the paper "A model to predict void-fraction in two-phase flow"[ I]. This model is based on a rather sophisticated assumption of parabolic void-fraction and liquid velocity profiles. Although it was shown121, 131 that the liauid velocitv orofde is less flat in