Horizontal tube evaporators: Part I. Theoretically-based correlations
β Scribed by G. Kocamustafaogullari; I.Y. Chen
- Publisher
- Elsevier Science
- Year
- 1989
- Tongue
- English
- Weight
- 436 KB
- Volume
- 16
- Category
- Article
- ISSN
- 0735-1933
No coin nor oath required. For personal study only.
β¦ Synopsis
Based on previous studies carried out by the authors, theoreticallybased correlations are developed for predicting the internal condensation and external evaporation heat transfer coefficients which can be used for the there1 perfor~nce of horizontal tube evaporators. It Is shown that the evaporation heat transfer outside tubes in a tube bundle can be correlated in terms of fi]m Reynolds nun~er, Prandtl number, dimensionless tube spacing, and pipe diameter.
It is also shown that the evaporation heat transfer in a tube bundle decreases from the first tube until a fully-developed region is reached. On the other hand, the condensation heat transfer inside tubes is correlated in terms of Kutateladze number, Galileo number, vapor and liquid phase superficial Reynolds number and the dimensionless pipe length.
Comparisons of the present predictions and experimental results are made and found to be in good agreement.
π SIMILAR VOLUMES
A simplified theoretical approach for the prediction of evaporation (nonucleate boiling) heat transfer coefficient in a horizontal tube falling film is proposed. The correlation is derived from an analysis of the thermal boundary layer under the assumption of turbulent flow regime and taking into ac
A new general flow pattern/flow structure based heat transfer model for condensation inside horizontal, plain tubes is proposed based on simplified flow structures of the flow regimes, and also includes the effect of liquid-vapor interfacial roughness on heat transfer. The model predicts local conde
Experiments of diabatic two-phase pressure drops in flow boiling were conducted in four horizontal flattened smooth copper tubes with two different heights of 2 and 3 mm. The equivalent diameters of the flat tubes are 8.6, 7.17, 6.25, and 5.3 mm. The working fluids are R22 and R410A, respectively. T