Accurate steady and unsteady numerical solutions of the full 2D governing equations—which model the forced film condensation flow of saturated vapor over a semi-infinite horizontal plate (the problem of Cess and Koh)—are obtained over a range of flow parameters. The results presented here are used to better understand the limitations of the well-known similarity solutions given by Koh. It is found that steady/quasisteady filmwise solution exists only if the inlet speed is above a certain threshold value. Above this threshold speed, steady/quasisteady film condensation solutions exist and their film thickness variations are approximately the same as the similarity solution given by Koh. However, these steady solutions differ from the Koh solution regarding pressure variations and associated effects in the leading part of the plate. Besides results based on the solutions of the full steady governing equations, this paper also presents unsteady solutions that characterize the steady solutions’ attainability, stability (response to initial disturbances), and their response to ever-present minuscule noise on the condensing-surface. For this shear-driven flow, the paper finds that if the uniform vapor speed is above a threshold value, an unsteady solution that begins with any reasonable initial-guess is attracted in time to a steady solution. This long time limiting solution is the same—within computational errors—as the solution of the steady problem. The reported unsteady solutions that yield the steady solution in the long time limit also yield “attraction rates” for nonlinear stability analysis of the steady solutions. The attraction rates are found to diminish gradually with increasing distance from the leading edge and with decreasing inlet vapor speed. These steady solutions are generally found to be stable to initial disturbances on the interface as well as in any flow variable in the interior of the flow domain. The results for low vapor speeds below the threshold value indicate that the unsteady solutions exhibit nonexistence of any steady limit of filmwise flow in the aft portion of the solution. Even when a steady solution exists, the flow attainability is also shown to be difficult (because of waviness and other sensitivities) at large downstream distances.

1.
Cess
,
R. D.
, 1960, “
Laminar Film Condensation on a Flat Plate in the Absence of a Body Force
,”
Z. Angew. Math. Phys.
0044-2275,
11
, pp.
426
433
.
2.
Koh
,
J. C. Y.
, 1962, “
Film Condensation in a Forced-Convection Boundary-Layer Flow
,”
Int. J. Heat Mass Transfer
0017-9310,
5
, pp.
941
954
.
3.
Rose
,
J. W.
, 1998, “
Condensation Heat Transfer Fundamentals
,”
Trans. Inst. Chem. Eng., Part A
0263-8762,
76
, pp.
143
152
.
4.
Balasubramaniam
,
R.
,
Nayagam
,
V.
,
Hasan
,
M. M.
, and
Khan
,
L.
, 2006, “
Analysis of Heat and Mass Transfer During Condensation Over a Porous Substrate
,”
Ann. N.Y. Acad. Sci.
0077-8923,
1077
, pp.
459
470
.
5.
Sparrow
,
E. M.
, and
Gregg
,
G. L.
, 1959, “
A Boundary Layer Treatment of Laminar Film Condensation
,”
ASME J. Heat Transfer
0022-1481,
81
, pp.
13
18
.
6.
Koh
,
J. C. Y.
,
Sparrow
,
E. M.
, and
Hartnett
,
J. P.
, 1961, “
The Two-Phase Boundary Layer in Laminar Film Condensation
,”
Int. J. Heat Mass Transfer
0017-9310,
2
, pp.
69
82
.
7.
Nusselt
,
W.
, 1916, “
Die Oberflächenkondesation des Wasserdampfes
,”
Z. Ver. Dtsch. Ing.
0341-7255,
60
(
27
), pp.
541
546
.
8.
Incropera
,
F. P.
, and
DeWitt
,
D. P.
, 1996,
Fundamentals of Heat and Mass Transfer
, 4th ed.,
Wiley
,
New York
.
9.
Mitra
,
S.
,
Narain
,
A.
,
Kulkarni
,
S.
,
Naik
,
R.
, and
Kurita
,
J. H.
, 2009, “
Annular/Stratified Internal Condensing Flows in Millimeter to Micrometer Scale Ducts
,”
Proceedings of the ASME Second Micro/Nanoscale Heat and Mass Transfer International Conference
, Shanghai, China, Dec. 18–22, Paper No. MNHMT 2009-18507.
10.
Rabas
,
T. J.
, and
Arman
,
B.
, 2000, “
Effects of the Exit Condition on the Performance of In-Tube Condensers
,”
Heat Transfer Eng.
0145-7632,
21
(
1
), pp.
4
14
.
11.
Chen
,
Y. P.
, and
Cheng
,
P.
, 2005, “
Condensation of Steam in Silicon Microchannels
,”
Int. Commun. Heat Mass Transfer
0735-1933,
32
, pp.
175
183
.
12.
Wu
,
H. Y.
, and
Cheng
,
P.
, 2005, “
Condensation Flow Patterns in Microchannels
,”
Int. J. Heat Mass Transfer
0017-9310,
48
, pp.
2186
2197
.
13.
Coleman
,
J. W.
, and
Garimella
,
S.
, 2003, “
Two-Phase Flow Regimes in Round, Square, and Rectangular Tubes During Condensation of Refrigerant R134a
,”
Int. J. Refrig.
0140-7007,
26
, pp.
117
128
.
14.
Garimella
,
S.
, 2004, “
Condensation Flow Mechanisms in Microchannels: Basis for Pressure Drop and Heat Transfer Models
,”
Heat Transfer Eng.
0145-7632,
25
, pp.
104
116
.
15.
Mitra
,
S. A.
,
Narain
,
R.
, and
Kulkarni
,
S. D.
, 2010, “
A Quasi One Dimensional Method and Results for Steady Annular/Stratified Shear and Gravity Driven Condensing Flows
,”
Int. J. Heat Mass Transfer
0017-9310, submitted.
16.
Phan
,
L.
, and
Narain
,
A.
, 2007, “
Nonlinear Stability of the Classical Nusselt Problem of Film Condensation and Wave Effects
,”
ASME J. Appl. Mech.
0021-8936,
74
(
2
), pp.
279
290
.
17.
Narain
,
A.
,
Kurita
,
J. H.
,
Kivisalu
,
M.
,
Siemionko
,
A.
,
Kulkarni
,
S.
,
Ng
,
T.
,
Kim
,
N.
, and
Phan
,
L.
, 2007, “
Internal Condensing Flows Inside a Vertical Pipe—Experimental/Computational Investigations of the Effects of Specified and Unspecified (Free) Exit Conditions at Exit
,”
ASME J. Heat Transfer
0022-1481,
129
, pp.
1352
1372
.
18.
Narain
,
A.
,
Liang
,
Q.
,
Yu
,
G.
, and
Wang
,
X.
, 2004, “
Direct Computational Simulations for Internal Condensing Flows and Results on Attainability/Stability of Steady Solutions, Their Intrinsic Waviness and Their Noise-Sensitivity
,”
ASME J. Appl. Mech.
0021-8936,
71
, pp.
69
88
.
19.
Liang
,
Q.
,
Wang
,
X.
, and
Narain
,
A.
, 2004, “
Effect of Gravity, Shear and Surface Tension in Internal Condensing Flows—Results From Direct Computational Simulations
,”
ASME J. Heat Transfer
0022-1481,
126
(
5
), pp.
676
686
.
20.
Phan
,
L.
,
Wang
,
X.
, and
Narain
,
A.
, 2006, “
Exit Condition, Gravity and Surface-Tension Effects on Stability and Noise Sensitivity Issues for Steady Condensing Flows Inside Tubes and Channels
,”
Int. J. Heat Mass Transfer
0017-9310,
49
(
13–14
), pp.
2058
2076
.
21.
Carey
,
V. P.
, 1992,
Liquid-Vapor Phase-Change Phenomena
(
Series in Chemical and Mechanical Engineering
),
Hemisphere Publication Corporation
,
New York
.
22.
Delhaye
,
J. M.
, 1974, “
Jump Conditions and Entropy Sources in Two-Phase Systems; Local Instant Formulation
,”
Int. J. Multiphase Flow
0301-9322,
1
, pp.
395
409
.
23.
Schlichting
,
H.
, 1968,
Boundary Layer Theory
, 6th ed.,
McGraw-Hill
,
New York
.
24.
Turner
,
J. S.
, 1973,
Buoyancy Effects in Fluids
,
Cambridge University Press
,
London
.
25.
Kundu
,
P. K.
, 1990,
Fluid Mechanics
,
Academic
,
San Diego, CA
.
26.
Gurtin
,
M. E.
, 1981,
An Introduction to Continuum Mechanics
,
Academic
,
New York
.
27.
Whitaker
,
S.
, 1977,
Fundamental Principles of Heat Transfer
,
Pergamon
,
New York
.
28.
Prasad
,
V.
, and
Jaluria
,
Y.
, 1982, “
Transient Film Condensation on Finite Horizontal Plate
,”
Chem. Eng. Commun.
0098-6445,
13
, pp.
327
342
.
You do not currently have access to this content.