Fuel droplets, formed by the interaction of fuel plumes with a water/fuel interface, can be discharged during the refueling of water-filled compensated fuel/ballast tanks. Motivated by increasingly stringent environmental regulations, a study was initiated to understand the physical mechanisms involved in the formation and transport of fuel droplets by complex immiscible flows inside a model tank. In particular, optical measurements were made of the size distribution of fuel droplets in water discharged from a three-bay model of a compensated fuel/ballast tank. The volumetric fuel concentration of discharge from the tank was inferred from measurements of droplet size and number. Flow visualizations inside the model were coupled to optical measurements of fuel droplets at the tank outlet to show that the presence of fuel in the discharged water was correlated to the formation of fuel plumes within the water-filled tank. The size distribution of fuel droplets at the tank exit is found to differ from the size distribution reported for the generation zone (near the fuel plumes) inside the tank. Thus, the advection of fuel droplets from the generation zone to the tank outlet is shown to affect the characteristics of discharged fuel droplets. The transport process specifically prevents large-diameter droplets from reaching the tank exit. Buoyancy tends to cause larger fuel droplets generated within the tank to rise and separate out of the flow before they can be discharged. The buoyancy time, τb(D), relative to the characteristic advection time, τa, of fuel droplets is a key parameter in predicting the fate of fuel droplets. The influence of buoyancy on the size distribution of discharged droplets was found to be modeled reasonably well by a Butterworth filter that depends on the ratio of timescales τaτb(D). This model, which relates the size distribution of discharged droplets to generated droplets, is found to produce the correct qualitative behavior that larger fuel droplets are discharged when the fuel plumes move closer to the tank exit, i.e., for decreasing advection time τa.

1.
Sathyagal
,
A. N.
,
Ramkrishna
,
D.
, and
Narsimhan
,
G.
, 1996, “
Droplet Breakage in Stirred Dispersions. Breakage Functions From Experimental Drop-Size Distributions
,”
Chem. Eng. Sci.
0009-2509,
51
, pp.
1377
1391
.
2.
Friedman
,
P. D.
, and
Katz
,
J.
, 1999, “
The Flow and Mixing Mechanisms Caused by the Impingement of an Immiscible Interface With a Vertical Jet
,”
Phys. Fluids
1070-6631,
11
, pp.
2598
2606
.
3.
Friedman
,
P. D.
,
Winthrop
,
A. L.
, and
Katz
,
J.
, 2001, “
Droplet Formation and Size Distributions From an Immiscible Interface Impinged With a Vertical Negatively Buoyant Jet
,”
Atomization Sprays
1044-5110
11
, pp.
269
290
.
4.
Wu
,
X.
, and
Katz
,
J.
, 1999, “
On the Flow Structures and Mixing Phenomenon in a Fuel/Water Stratified Shear Flow
,”
Proc. ASME/JSME Joint Fluids Engineering Conference
,
San Diego, CA
, July 18–23.
5.
Chang
,
P. A.
,
Atsavapranee
,
P.
,
McGinn
,
J.
, and
Hwang
,
W.
, 2001, “
Buoyant Flow Event Experiments in a Half-Scale, Two-Bay Model of a Compensated Fuel/Ballast Tank
,” Hydro. Dir. Tech. Report NSWCCD-50-TR-2001/032, Nav. Surf. War. Cnt., Carderock Div., May.
6.
Atsavapranee
,
P.
,
Verosto
,
S.
, and
Shan
,
J. W.
, 2003, “
Experimental Techniques to Determine Oil-in-Water Concentrations During Compensated Fuel Ballast Refueling Tests
,”
Proc. ASME/SNAME Marine Env. Eng. Tech. Symp (MEETS)
.
7.
Chen
,
C. J.
, and
Rodi
,
W.
, 1980,
Vertical Turbulent Buoyant Jets
,
Pergamon Press
, Oxford.
8.
Dimotakis
,
P. E.
, 2000, “
The Mixing Transition in Turbulence
,”
J. Fluid Mech.
0022-1120,
409
, pp.
69
98
.
9.
Batchelor
,
G. K.
, 1967,
An Introduction to Fluid Dynamics
,
Cambridge University Press
, Cambridge.
10.
Clift
,
R.
,
Grace
,
J. R.
, and
Weber
,
M. E.
, 1978,
Bubbles, Drops, and Particles
,
Academic Press
, New York.
11.
Kulenovic
,
R.
,
Mertz
,
R.
, and
Groll
,
M.
, 2002, “
High Speed Flow Visualization of Pool Boiling From Structured Tubular Heat Transfer Surfaces
,”
Exp. Therm. Fluid Sci.
0894-1777,
25
, pp.
547
555
.
12.
Atsavapranee
,
P.
,
Chang
,
P. A.
,
Wilson
,
W.
, and
Verosto
,
S.
, 2002, “
Effluent Fuel Concentration Measurements in a Half-Scale, Three-Bay Compensated Fuel/Ballast Tank
,” Hydro. Dir. Tech. Report NSWCCD-50-TR-2002/021, Nav. Surf. War. Cnt., Carderock Div., April.
13.
Martínez-Bazán
,
C.
, and
Lasheras
,
J. C.
, 2001, “
Turbulent Dispersion of Bubbles in a Plane, Free Shear Layer
,”
Exp. Therm. Fluid Sci.
0894-1777,
25
, pp.
437
445
.
14.
Acheson
,
D. J.
, 1990,
Elementary Fluid Dynamics
,
Oxford Univ. Press
, Oxford.
15.
Takagi
,
S.
, and
Matsumoto
,
Y.
, 2000, “
Contaminant Effect on the Motion of a Rising Bubble
,”
Proc. ASME Fluids Engineering Division Summer Meeting
,
Boston, MA
, July 11–15.
16.
White
,
F. M.
, 1991,
Viscous Fluid Flow
,
McGraw-Hill
, New York.
17.
Friedman
,
P. D.
, and
Katz
,
J.
, 2001, “
Dispersion of Fuel Droplets in Isotropic Turbulence
,” 4th Int. Conf. Multiphase Flow, New Orleans, LA, May 27–April 1.
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