The effects of insulated and isothermal thin baffles on pseudosteady-state natural convection within spherical containers were studied computationally. The computations are based on an iterative, finite-volume numerical procedure using primitive dependent variables. Natural convection effect is modeled via the Boussinesq approximation. Parametric studies were performed for a Prandtl number of 0.7. For Rayleigh numbers of 104, 105, 106, and 107, baffles with three lengths positioned at five different locations were investigated (120 cases). The fluid that is heated adjacent to the sphere rises replacing the colder fluid, which sinks downward through the stratified stable thermal layer. For high Ra number cases, the hot fluid at the bottom of the sphere is also observed to rise along the symmetry axis and encounter the sinking colder fluid, thus causing oscillations in the temperature and flow fields. Due to flow obstruction (blockage or confinement) effect of baffles and also because of the extra heating afforded by the isothermal baffle, multi-cell recirculating vortices are observed. This additional heat is directly linked to creation of another recirculating vortex next to the baffle. In effect, hot fluid is directed into the center of the sphere disrupting thermal stratified layers. For the majority of the baffles investigated, the Nusselt numbers were generally lower than the reference cases with no baffle. The extent of heat transfer modification depends on Ra, length, and location of the extended surface. With an insulated baffle, the lowest amount of absorbed heat corresponds to a baffle positioned horizontally. Placing a baffle near the top of the sphere for high Ra number cases can lead to heat transfer enhancement that is linked to disturbance of the thermal boundary layer. With isothermal baffles, heat transfer enhancement is achieved for a baffle placed near the bottom of the sphere due to interaction of the counterclockwise rotating vortex and the stratified layer. For some high Ra cases, strong fluctuations of the flow and thermal fields indicating departure from the pseudosteady-state were observed.

1.
Schmidt
,
E.
, 1956, “
Versuche zum Wärmeübergang bei natürlicher Konvektion
,”
Chem.–Ing.–Tech.
,
28
(
3
), pp.
175
180
.
2.
Shaidurov
,
G. F.
, 1958, “
On Convective Heat Transfer Across a Spherical Cavity
,”
Sov. Phys. Tech. Phys.
0038-5662,
3
(
4
), pp.
799
804
.
3.
Pustovoit
,
S. P.
, 1958, “
Transient Thermal Convection in a Spherical Cavity
,”
J. Appl. Math. Mech.
0021-8928,
22
(
4
), pp.
800
806
.
4.
Whitley
,
H. G.
, III
, and
Vachon
,
R. I.
, 1972, “
Transient Laminar Free Convection in Closed Spherical Containers
,”
ASME J. Heat Transfer
0022-1481,
94
, pp.
360
366
.
5.
Chow
,
M. Y.
, and
Akins
,
R. G.
, 1975, “
Pseudosteady-State Natural Convection Inside Spheres
,”
ASME J. Heat Transfer
0022-1481,
97
, pp.
54
59
.
6.
Zhang
,
Y.
,
Khodadadi
,
J. M.
, and
Shen
,
F.
, 1999, “
Pseudosteady-State Natural Convection Inside Spherical Containers Partially Filled With a Porous Medium
,”
Int. J. Heat Mass Transfer
0017-9310,
42
(
13
), pp.
2327
2336
.
7.
Val’tsiferov
,
Y. V.
, and
Polezhaev
,
V. I.
, 1975, “
Convective Heat Transfer and Temperature Stratification in a Sphere Completely Filled With a Liquid, With a Given Heat Flux
,”
Fluid Dyn.
0015-4628,
10
(
5
), pp.
828
832
.
8.
Hutchins
,
J.
, and
Marschall
,
E.
, 1989, “
Pseudosteady-State Natural Convection Heat Transfer Inside Spheres
,”
Int. J. Heat Mass Transfer
0017-9310,
32
(
11
), pp.
2047
2053
.
9.
Shen
,
F.
,
Khodadadi
,
J. M.
, and
Zhang
,
Y.
, 1995, “
Pseudosteady-State Natural Convection Inside Spherical Containers
,”
Proceedings of the Fourth ASME/JSME Thermal Engineering Joint Conference
, Lahaina, Maui, HI, Vol.
1
, pp.
209
216
.
10.
Khodadadi
,
J. M.
,
Li
,
W.
, and
Shi
,
X.
, 1999, “
Pseudosteady-State Mixed Convection Inside Rotating Spherical Containers
,”
Proceedings of the Fifth ASME/JSME Thermal Engineering Joint Conference (CD ROM)
, Paper No. AJTE99-6264, San Diego, CA.
11.
Shi
,
X.
, and
Khodadadi
,
J. M.
, 2003, “
Laminar Natural Convection Heat Transfer in a Differentially Heated Square Cavity due to a Thin Fin on the Hot Wall
,”
ASME J. Heat Transfer
0022-1481,
125
(
4
), pp.
624
634
.
12.
Patankar
,
S. V.
, 1980,
Numerical Heat Transfer and Fluid Flow
,
Hemisphere
,
Washington, DC
.
13.
Fluent, Inc.
, 2003, FLUENT 6.1 User’s Guide, NH, Lebanon.
14.
Duan
,
Y.
, 2007, “
Effect of a Baffle on Pseudosteady-State Natural Convection Inside Spherical Containers
,” MS thesis, Department of Mechanical Engineering, Auburn University; available at http://etd.auburn.edu/etdhttp://etd.auburn.edu/etd.
15.
Owen
,
I.
, and
Jalil
,
J. M.
, 1986, “
Transient Heat Transfer in a Liquid Sphere
,”
Heat Transfer 1986: Proceedings of the Eight International Heat Transfer Conference
,
Taylor & Francis
,
London
, Vol.
4
, pp.
1889
1893
.
You do not currently have access to this content.