A mechanistic model for the boiling heat flux prediction proposed in Part I of this two-part paper (2009, “A Statistical Model of Bubble Coalescence and Its Application to Boiling Heat Flux Prediction—Part I: Model Development,” ASME J. Heat Transfer, 131, p. 121013) is verified in this part. In the first step, the model is examined by experiments conducted using R134a covering a range of pressures, inlet subcoolings, and flow velocities. The density of the active nucleation sites is measured and correlated with critical diameter Dc and static contact angle θ. Underlying submodels on bubble growth and bubble departure/lift-off radii are validated. Predictions of heat flux are compared with the experimental data with an overall good agreement observed. This model achieves an average error of ±25% for the prediction of R134a boiling curves, with the predicted maximum surface heat flux staying within ±20% of the experimentally measured critical heat flux. In the second step, the model is applied to water data measured by McAdams et al. (1949, “Heat Transfer at High Rates to Water With Surface Boiling,” Ind. Eng. Chem., 41(9), pp. 1945–1953) in vertical circular tubes. The consistency suggests that the application of this mechanistic model can be extended to other flow conditions if the underlying submodels are appropriately chosen and the assumptions made during model development remain valid.

1.
Wu
,
W.
,
Jones
,
B. G.
, and
Newell
,
T. A.
, 2009, “
A Statistical Model of Bubble Coalescence and Its Application to Boiling Heat Flux Prediction—Part I: Model Development
,”
ASME J. Heat Transfer
0022-1481,
131
(
12
), p.
121013
.
2.
Basu
,
N.
,
Warrier
,
G. R.
, and
Dhir
,
V. K.
, 2002, “
Onset of Nucleate Boiling and Active Nucleation Site Density During Subcooled Flow Boiling
,”
ASME J. Heat Transfer
0022-1481,
124
, pp.
717
728
.
3.
Fitzgibbon
,
A.
,
Pilu
,
M.
, and
Fisher
,
R. B.
1999, “
Direct Least Squares Fitting of Ellipses
,”
IEEE Trans. Pattern Anal. Mach. Intell.
0162-8828,
21
(
5
), pp.
476
480
.
4.
Taubin
,
G.
, 1991, “
Estimation of Planar Curves, Surfaces and Non-Planar Space Curves Defined by Implicit Equations, With Applications to Edge and Range Image Segmentation
,”
IEEE Trans. Pattern Anal. Mach. Intell.
0162-8828,
13
(
11
), pp.
1115
1138
.
5.
Wu
,
W.
,
Chen
,
P.
,
Jones
,
B. G.
, and
Newell
,
T. A.
, 2008, “
A Study on Bubble Detachment and the Impact of Heated Surface Structure in Subcooled Nucleate Boiling Flows
,”
Nucl. Eng. Des.
0029-5493,
238
(
10
), pp.
2693
2698
.
6.
Mikic
,
B. B.
,
Rohsenow
,
W. M.
, and
Griffith
,
P.
, 1970, “
On Bubble Growth Rates
,”
Int. J. Heat Mass Transfer
0017-9310,
13
, pp.
657
666
.
7.
Thorncroft
,
G. E.
,
Klausner
,
J. F.
, and
Mei
,
R.
, 2001, “
Bubble Forces and Detachment Models
,”
Multiphase Sci. Technol.
0276-1459,
13
(
3&4
), pp.
35
76
.
8.
McAdams
,
W. H.
,
Kennel
,
W. E.
,
Minden
,
C. S.
,
Carl
,
R.
,
Picornell
,
P. M.
, and
Dew
,
J. E.
, 1949, “
Heat Transfer at High Rates to Water With Surface Boiling
,”
Ind. Eng. Chem.
0019-7866,
41
(
9
), pp.
1945
1953
.
9.
Basu
,
N.
,
Warrier
,
G. R.
, and
Dhir
,
V. K.
, 2005, “
Wall Heat Flux Partitioning During Subcooled Flow Boiling: Part II—Model Validation
,”
ASME J. Heat Transfer
0022-1481,
127
, pp.
141
148
.
10.
Kandlikar
,
S. G.
, 1997, “
Further Developments in Subcooled Flow Boiling Heat Transfer
,”
Engineering Foundation Conference on Convective and Pool Boiling
, Irsee, Germany, May 18–25.
You do not currently have access to this content.