Skip to main content
Log in

A modified heat transfer correlation for two-phase flow

  • Original
  • Published:
Heat and Mass Transfer Aims and scope Submit manuscript

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.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Fig. 1
Fig. 2
Fig. 3
Fig. 4
Fig. 5
Fig. 6
Fig. 7
Fig. 8
Fig. 9

Similar content being viewed by others

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

References

  1. Kim J, Ghajar AJ (2006) A general heat transfer correlation for non-boiling gas-liquid flow with different flow patterns in horizontal pipes. Int J Multiph Flow 32(4):447–465

    Article  MATH  Google Scholar 

  2. Hetsroni G, Hu BG, Yi BG, Mosyak A, Yarin LP, Ziskind G (1998) Heat transfer in intermittent air-water flow—part I: horizontal tube. Int J Multiph Flow 24(2):165–188

    Article  MATH  Google Scholar 

  3. Hetsroni G, Hu BG, Yi BG, Mosyak A, Yarin LP, Ziskind G (1998) Heat transfer in intermittent air-water flow—Part II: upward inclined tube. Int J Multiph Flow 24(2):188–212

    Google Scholar 

  4. Mosyak A, Hetsroni G (1999) Analysis of dryout in horizontal and inclined tubes. Int J Multiph Flow 25(8):1521–1543

    Article  MATH  Google Scholar 

  5. Kaminsky RD (1999) Estimation of two-phase flow heat transfer in pipes. J Energy Resour Technol 121(2):75–80

    Article  Google Scholar 

  6. Kutz M (2006) Heat transfer calculation. McGraw Hill, NY, pp 23.1–25.18

  7. Kim D, Ghajar AJ, Dougherty RL, Ryali VK (1999) Comparison of 20 two-phase heat transfer correlations with seven sets of experimental data, including flow pattern and tube inclination effects. Heat Transf Eng 20(1):15–40

    Article  Google Scholar 

  8. Rezkallah KS, Sims GE (1987) An examination of correlations of mean heat transfer coefficients in two-phase and two-component flow in vertical tubes. AIChE Symp Ser 83:109–114

    Google Scholar 

  9. Chu YC, Jones BG (1980) Convective heat transfer coefficient studies in upward and downward, vertical, two-phase, non-boiling flows. AIChE Symp Ser 76:79–90

    Google Scholar 

  10. Vijay MM, Aggour MA, Sims GE (1982) A correlation of mean heat transfer coefficients for two-phase two-component flow in a vertical tube. Proceedings of 7th international heat transfer conference vol 5, pp 367–372

  11. Knott RF, Anderson RN, Acrivos A, Petersen EE (1959) An experimental study of heat transfer to Nitrogen-Oil mixtures. Ind Eng Chem 51:1369–1372

    Article  Google Scholar 

  12. Martin BW, Sims GE (1971) Forced convection heat transfer to water with air injection in a rectangular duct. Int J Heat Mass Transf 14:1115–1134

    Article  Google Scholar 

  13. Shah MM (1981) Generalized prediction of heat transfer during two-component gas-liquid flow in tubes and other channels. AIChE Symp Ser 77:140–151

    Google Scholar 

  14. Kim D, Ghajar AJ, Dougherty RL (2000) Robust heat transfer correlation for turbulent gas-liquid flow in vertical pipes. J Thermophys Heat Trans 14:574–578

    Article  Google Scholar 

  15. Holman JP (1986) Heat transfer, 6.th edn. McGraw Hill book company, NY

    Google Scholar 

  16. Vaze MJ, Banerjee J (2011) Experimental visualization of two-phase flow patterns and transition from stratified to slug flow. Proc Inst Mech Eng C J Mech Eng Sci 225:382–389

  17. UKAS (United Kingdom Accreditation Service) (2007) The expression of uncertainty and confidence in measurement, M3003, 2nd edn

  18. Davis EJ, David MM (1964) Two-phase gas-liquid convention heat transfer. Ind Eng Chem Fundam 3(2):111–118

    Article  Google Scholar 

  19. Hughmark GA (1965) Holdup and heat transfer in horizontal slug gas-liquid flow. Chem Eng Sci 20:1007–1010

    Article  Google Scholar 

  20. Oliver DR, Wright SJ (1964) Pressure drop and heat transfer in gas-liquid slug flow in horizontal tubes. Br Chem Eng 9:590–596

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Jyotirmay Banerjee.

Rights and permissions

Reprints and permissions

About this article

Cite this article

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

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s00231-011-0784-x

Keywords

Navigation