Abstract
Experimental investigations for two-phase flow under constant heat flux condition are carried out by varying the mass flow rate of gas and liquid phases. A modified correlation for Nusselt number is developed based on the experimental measurements involving superficial gas and liquid Reynolds number, fluid properties and Lockhart-Martinelli parameter. The accuracy of this correlation for all two-phase flow regimes is validated with the recent correlation proposed by Kim and Ghajar.
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Abbreviations
- A:
-
Cross-sectional area, m2
- c :
-
Specific heat at constant pressure, KJ/kg K
- C :
-
Constant
- dz :
-
Distance between two RTD stations, m
- D :
-
Diameter, m
- F p :
-
Flow pattern factor
- F s :
-
Shape factor
- g :
-
Gravitational acceleration, m/s2
- G t :
-
Mass velocity of total flow, kg/m2s
- h :
-
Convective heat transfer coefficient, W/m2 K
- I :
-
Inclination factor
- k :
-
Thermal conductivity, W/m K
- L :
-
Length of test section, m
- m, n, p, q, r :
-
Exponents
- \( \dot{m} \) :
-
Mass flow rate, kg/s
- p :
-
Pressure, Pa
- ∆P/∆L :
-
Total pressure drop per unit length, Pa/m
- \( \dot{q}^{\prime \prime } \) :
-
Heat supplied per unit area, W/m2
- Q :
-
Volumetric flow rate, m3/s
- ΔT :
-
Temperature difference, °C
- R L :
-
Liquid volume fraction, (1-α)
- V :
-
Velocity, m/s
- x :
-
Mass fraction
- X :
-
Lockhart-Martinelli parameter
- α :
-
Volume fraction
- θ :
-
Inclination angle
- μ :
-
Absolute viscosity, kg/m s
- ρ :
-
Density, kg/m3
- σ :
-
Surface tension, N/s
- 1, 2, 3, 4 :
-
Station number
- avg :
-
Average
- b :
-
Bulk
- bi, bo :
-
Bulk in, bulk out
- exp:
-
Experiment
- g, l :
-
Gas, liquid
- SG, SL:
-
Superficial gas, superficial liquid
- t :
-
Total
- TP:
-
Two-phase
- w :
-
Wall
- z :
-
RTD station
- A:
-
Annular flow
- B:
-
Bubbly flow
- Eo:
-
Eotvos number
- F:
-
Froth flow
- M:
-
Mist flow
- Nu:
-
Nusselt number
- P:
-
Plug flow
- Pr:
-
Prandtl number
- Re:
-
Reynolds number
- RTD:
-
Resistance temperature detector
- S:
-
Slug flow
- St:
-
Stratified flow
- SW:
-
Slug/wavy flow
- SBA:
-
Slug/bubbly/annular flow
- W:
-
Wavy flow
- WA:
-
Wavy/annular flow
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Vaze, M.J., Banerjee, J. A modified heat transfer correlation for two-phase flow. Heat Mass Transfer 47, 1159–1170 (2011). https://doi.org/10.1007/s00231-011-0784-x
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DOI: https://doi.org/10.1007/s00231-011-0784-x