A dewce for studying hydrodynamics and heat transfer m hehum flow (hehum being m two-phase hquld, and supercrtbcal states) ts descrtbed Prehmmary data about pressure drop and heat transfer in two-phase hehum flow are presented. The tube used was about 0 45 mm I d and about I m long. The mass flow m
A separated flow model for predicting two-phase pressure drop and evaporative heat transfer for vertical annular flow
โ Scribed by Feng Fu; James F. Klausner
- Publisher
- Elsevier Science
- Year
- 1997
- Tongue
- English
- Weight
- 890 KB
- Volume
- 18
- Category
- Article
- ISSN
- 0142-727X
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โฆ Synopsis
A separated flow model has been developed that is applicable to vertical annular two-phase flow in the purely convective heat transfer regime. Conservation of mass, momentum, and energy are used to solve for the liquid film thickness, pressure drop, and heat transfer coefficient. Closure relationships are specified for the interfacial friction factor, liquid film eddy-viscosity, turbulent Prandtl number, and entrainment rate. Although separated flow models have been reported previously, their use has been limited, because they were tested over a limited range of flow and thermal conditions. The unique feature of this model is that it has been tested and calibrated against a vast array of two-phase pressure drop and heat transfer data, which include upflow, downflow, and microgravity flow conditions. The agreemsents between the measured and predicted pressure drops and heat transfer coefficients are, on average, better or comparable to the most reliable empirical correlations. This separated flow model _is demonstrated to be a reliable and practical predictive tool for computing two-phase pressure drop and heat transfer rates. All of the datasets have been obtained from the open literature.
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