A general correlation for saturated two-phase flow boiling heat transfer inside horizontal and vertical tubes
- Rochester Inst. of Tech., NY (United States)
A simple correlation was developed earlier by Kandlikar (1983) for predicting saturated flow boiling heat transfer coefficients inside horizontal and vertical tubes. It was based on a model utilizing the contributions due to nucleate boiling and convective mechanisms. It incorporated a fluid-dependent parameter F{sub fl} in the nucleate boiling term. The predictive ability of the correlation for different refrigerants was confirmed by comparing it with the recent data on R-113 by Jensen and Bensler (1986) and Khanpara et al. (1986). In the present work, the earlier correlation is further refined by expanding the data base to 5,246 data points from 24 experimental investigations with ten fluids. The proposed correlation gives a mean deviation of 15.9 percent with water data, and 18.8 percent with all refrigerant data, and it also predicts the correct h{sub TP} versus x trend as verified with water and R-113 data yielded the lowest mean deviations among correlations tested. The proposed correlation can be extended to other fluids by evaluating the fluid-dependent parameter F{sub fl} for that fluid from its flow boiling or pool boiling data.
- OSTI ID:
- 5633093
- Journal Information:
- Journal of Heat Transfer (Transactions of the ASME (American Society of Mechanical Engineers), Series C); (United States), Vol. 112:1; ISSN 0022-1481
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
HEAT TRANSFER
MATHEMATICAL MODELS
TUBES
CONVECTION
FREONS
NUCLEATE BOILING
ORIENTATION
REFRIGERANTS
TWO-PHASE FLOW
BOILING
ENERGY TRANSFER
FLUID FLOW
FLUIDS
HALOGENATED ALIPHATIC HYDROCARBONS
MASS TRANSFER
ORGANIC COMPOUNDS
ORGANIC HALOGEN COMPOUNDS
PHASE TRANSFORMATIONS
WORKING FLUIDS
420400* - Engineering- Heat Transfer & Fluid Flow