Erratum: Performance of smooth and micro-fin tubes in high mass flux region of R-134a during evaporation (Heat and Mass Transfer/Waerme - und Stoffuebertragung (2002) DOI: 10.1007/s00231-002-0397-5));Performance of smooth and micro-fin tubes in high mass flux region of R-134a during evaporation

Heat and Mass Transfer/Waerme- und Stoffuebertragung

Volumn 40, Issue 6-7, 2004, Pages 425-435

  Wongsa Ngam, Jittraporn ^a   Nualboonrueng, Thipjak ^a   Wongwises, Somchai ^a  

^a KING MONGKUT'S UNIVERSITY OF TECHNOLOGY THONBURI   (Thailand)

Author keywords

Evaporation; Heat transfer coefficient; Micro fin tube; Pressure drop; Smooth tube; Two phase

Indexed keywords

EVAPORATION; FRICTION; PRANDTL NUMBER; PRESSURE DROP; PRESSURE EFFECTS; THERMAL CONDUCTIVITY; VISCOSITY;

MASS FLUX; MICRO-FIN TUBES; SPIRAL ANGLE; TWO-PHASE MULTIPLIERS;

HEAT TRANSFER;

EID: 21044451766     PISSN: 09477411     EISSN: 14321181     Source Type: Journal    
DOI: 10.1007/s00231-002-0408-6     Document Type: Erratum

References (17)

1. Schlager LM; Pate MB; Bergles AE (1990) Evaporation and condensation heat transfer and pressure drop in horizontal 12.7 mm micro-fin tubes with refrigerant 22. J Heat Transfer 112: 1041-1047
2. Eckels SJ; Pate MB (1991) Evaporation and condensation of HFC-134a and CFC-12 in a smooth tube and a micro-fin tube. ASHRAE Transaction pp 71-81
3. Eckels SJ; Doerr TM; Pate MB (1995) In-tube heat transfer and pressure drop of R-134a and ester lubricant mixtures in a smooth tube and a micro-fin tube. Part I-evaporation. ASHRAE Transaction pp 265-282
4. Eckels SJ; Doerr TM; Pate MB (1998) Heat transfer coecients and pressure drops for R-134a and an ester lubricant mixture in a smooth tube and a micro-fin tube. ASHRAE Transaction pp 366-375
5. Kuo CS; Wang CC (1996) In-tube evaporation of HCFC-22 in a 9.52 mm micro-fin/smooth tube. Int J Heat Mass Transfer 39: 2559-2569
6. Kandlikar SG; Rayko T (1996) Predicting flow boiling heat transfer for refrigerants in microfin tubes. Proc 2nd European Thermal-Science 14th UIT National Heat Transfer Conference 1996, Vol. 1, Edizioni ETS, Pisa, Italy pp 475-482
7. Lallemand M; Branescu C; Haberschil P (2001) Local heat transfer coecient during boiling R-22 and R-407C in horizontal smooth and micro-fin tubes. Int J Refrigeration 24: 57-72
8. Chaddock JB; Noerager JA (1966) Evaporation of refrigerant 12 in a horizontal tube with constant wall heat flux. ASHRAE Transactions 72: 90-101
9. Shah MM (1982) Chart correlation for saturated boiling heat transfer equation and further study. ASHRAE Transactions 88: 185-196
10. Gungor KE; Winterton RHS (1986) A general correlation for flow boiling in tubes and annuli. Int J Heat Mass Transfer 29: 351-358
11. Kandlikar SG (1990) A general correlation for predicting the two-phase flow boiling heat transfer coecient inside horizontal and vertical tubes. J Heat Transfer 102: 219-228
12. Chisholm D (1973) Pressure gradients due to friction during the flow of evaporating two-phase mixtures in smooth tubes and channels. Int J Heat Mass Transfer 16: 347-358
13. Friedel L (1979) Improve friction pressure drop correlations for horizontal and vertical two-phase pipe flow. Paper presented at the European Two-phase Flow Group Meeting, Ispra, Italy, Paper E
14. Chisholm D (1967) A theoretical basis for the Lockhart-Martinelli correlation for two-phase flow. Int J Heat Mass Transfer 10:1767-1778
15. Cavallini A; Del Col D; Doretti L; Longo GA; Rossetto L (1997) Pressure drop during condensation and vaporization of refrigerants inside enhanced tubes. Heat and Technology 15: 3-10
16. Choi JY; Kedzierski MA; Domanski PA (1999) A generalized pressure drop correlation for evaporation and condensation of alternative refrigerants in smooth and micro-fin tubes. NI-STIR6333 pp 8-18
17. Miller RW (1983) Flow measurement engineering handbook. New York. McGraw-Hill