Difficulties are experienced during the thermal–hydraulic design of a nuclear reactor operating in the transition flow regime and are the result of the inability to accurately predict the heat transfer coefficient (HTC). Experimental values for the HTC in rectangular channels are compared with the calculated by correlations usually used for the design of material testing reactors (MTR). The values predicted by Gnielinski and Kreith correlations at Reynolds numbers below 5000 are not necessarily conservative. The Al-Arabi-Churchill correlation with the correction proposed by Jones has proved to be conservative for Reynolds between 2100 and 5000. Two alternative design approaches are proposed to solve a specific thermal–hydraulic design problem for a MTR operating at Reynolds 2500. The conservative approach comprises two alternatives: the use of Al-Arabi correlation with no uncertainty factors, as it has proved to be conservative, or the use of Kreith correlation with a maximum uncertainty. In this conservative approach, maximum deviations in other input parameters are also taken into account. The best estimate plus uncertainty approach considers an uncertainty distribution in input parameters to generate a random sample of 59 inputs. An uncertainty distribution based on the ratio between the experimental and the calculated HTC, when using Kreith correlation, is considered. Results are given in terms of maximum and minimum bounds for the figure of merit used as design criterion with 95% probability and 95% confidence level. The best estimate plus uncertainty approach offers a less penalizing design and its use depends on regulator's acceptance.

References

1.
Gnielinski
,
V.
,
1976
, “
New Equations for Heat and Mass Transfer in Turbulent Pipe and Channel Flow
,”
Int. Chem. Eng.
,
16
(
2
), pp.
359
368
.
2.
Petukhov
,
B. S.
,
1970
, “
Heat Transfer and Friction in Turbulent Pipe Flow With Variable Physical Properties
,”
Advances in Heat Tranfer
,
J. P.
Hartnett
and
T. F.
Irvine
. Jr., (eds.), Vol.
50
,
Academic Press
,
New York
, pp.
503
564
.
3.
Sieder
,
E. N.
, and
Tate
,
G. E.
,
1936
, “
Heat Transfer and Pressure Drop of Liquids in Tubes
,”
Ind. Eng. Chem.
,
28
(
12
), pp.
1429
1435
.
4.
Silin
,
N.
,
Masson
,
V. P.
, and
Marino
,
R.
,
2012
, “
Heat Transfer in a Short Parallel-Plate Channel in the Transition Regime
,”
Exp. Heat Transfer
,
25
(
1
), pp.
12
29
.
5.
Sleicher
,
C. A.
, and
Rouse
,
M. W.
,
1975
, “
A Convenient Correlation for Heat Transfer to Constant and Variable Property Fluids in Turbulent Pipe Flow
,”
Int. J. Heat Mass Transfer
,
18
(
5
), pp.
677
683
.
6.
Kreith
,
F.
,
1969
,
Principles of Heat Transfer
,
International Textbook Company
,
Pennsylvania, PA
, Chap. 8.
7.
Information Systems Laboratories
,
2010
, “
RELAP3.3 MOD 3 Code Manual Volume IV: Models and Correlations
,” Information Systems Laboratories, Inc., Rockville, MD, Prepared for the Division of Systems Research, Office of Nuclear Regulatory Research, U. S. Nuclear Regulatory Commission, Washington, DC.
8.
TERMIC V. 4.4
,
2002
, “
TERMIC V. 4.4. A Program for the Thermal-hydraulic Analysis of a MTR Core in Forced Convection
,” Manual to be used by INVAP S.E., San Carlos de Bariloche,
Argentina
(unpublished).
9.
Al-Arabi
,
M.
,
1982
, “
Turbulent Heat Transfer in the Entrance Region of a Tube
,”
Heat Transfer Eng.
,
4
(
3
), pp.
76
83
.
10.
Churchill
,
S. W.
,
1977
, “
Comprehensive Correlating Equations for Heat, Mass and Momentum Transfer in Fully Developed Flow in Smooth Tubes
,”
Ind. Chem. Fundam.
,
16
(
1
), pp.
109
116
.
11.
Kakac
,
S.
,
Shah
,
R.
, and
Aung
,
W.
,
1987
,
Handbook of Single-Phase Convective Heat Transfer
,
Wiley
,
New York
.
12.
Jones
,
O. C.
, Jr.
,
1976
, “
An Improvement in the Calculation of Turbulent Friction in Rectangular Ducts
,”
ASME J. Fluids Eng.
,
98
(
2
), pp.
173
181
.
13.
Wilks
,
S. S.
,
1941
, “
Determination of Sample Sizes for Setting Tolerance Limits
,”
Ann. Math. Stat.
,
12
(
1
), pp.
91
96
.
14.
Wilks
,
S. S.
,
1942
, “
Statistical Prediction With Special Reference to the Problem of Tolerance Limits
,”
Ann. Math. Stat.
,
13
(
4
), pp.
400
409
.
15.
D'Auria
,
F.
, and
Petruzzi
,
A.
, 2008, “
Background and Qualification of Uncertainty Methods
,”
THICKET 2008-Session VI
, University of Pisa, Pisa, Italy, Paper No. 15.https://inis.iaea.org/collection/NCLCollectionStore/_Public/42/101/42101987.pdf
16.
Machaca Abregu
,
W. I.
, and
Teruel
,
F. E.
,
2016
, “
Transferencia de Calor en el Régimen de Transición Laminar–turbulento en Canales Rectangulares Para Reynolds Moderados
,” Mecánica Computacional, Córdoba, Spain, Nov. 8–11, pp.
1859
1868
.
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