1965
DOI: 10.1115/1.3689054
|View full text |Cite
|
Sign up to set email alerts
|

Effect of Large Temperature Gradients on Convective Heat Transfer: The Downstream Region

Abstract: The results of an experimental investigation of the frictional and heat transfer effects in air, nitrogen, and helium in steady, turbulent flow in round tubes are presented. Wall-to-bulk temperature ratios extend from near unity to 2.5, entering Reynolds numbers from 15,000 to 233,000. Dependence of the thermodynamic and transport properties on temperature is shown to be significant in both heat transfer and wall friction and is reflected in the empirical correlations for local and average coefficients which a… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

2
31
0

Year Published

1966
1966
2022
2022

Publication Types

Select...
3
3
2

Relationship

0
8

Authors

Journals

citations
Cited by 69 publications
(33 citation statements)
references
References 0 publications
2
31
0
Order By: Relevance
“…The best agreement was obtained with the correlations of Petukhov and Popov (1963) and McEligot et al (1965) for friction coefficient and Nusselt number, respectively. However, the simulations of cases 2-6 don't agree as well with the correlations as case 1.…”
Section: Friction Coefficient and Nusselt Numbersupporting
confidence: 70%
See 1 more Smart Citation
“…The best agreement was obtained with the correlations of Petukhov and Popov (1963) and McEligot et al (1965) for friction coefficient and Nusselt number, respectively. However, the simulations of cases 2-6 don't agree as well with the correlations as case 1.…”
Section: Friction Coefficient and Nusselt Numbersupporting
confidence: 70%
“…The region of interest in this research is the "quasi-developed" region (McEligot et al, 1965), where thermal entry effects are no longer important.…”
Section: (Mceligot Et Al (1998))mentioning
confidence: 99%
“…CFD validation calculations will be performed based on available mixed convection data [McEligot, Magee, and Leppert 1965;Perkins and McEligot 1975;Reynolds 1968;Shumway 1969;Vilemas and Poskas 1999;Bae et al 2004] to demonstrate the capability of the CFD tools to adequately calculate the appropriate fluid and heat transfer behavior. Following validation, a CFD code may be used during FY-07 to evaluate the core heat transfer in conjunction with the flow distributions in the lower and upper plenums to calculate the potential for localized hot spots in the vessel upper head and control rod apparatus (see Section 4.3.10).…”
Section: Thermal-hydraulic Design Methods Development Validation Anmentioning
confidence: 99%
“…Also, the correlations developed on the basis of available mixed convection data [McEligot, Magee, and Leppert 1965;Perkins and McEligot 1975;Reynolds 1968;Shumway 1969;Vilemas and Poskas 1999;Bae et al 2004] will be evaluated for applicability and installed in the systems analysis software.…”
Section: Thermal-hydraulic Design Methods Development Validation Anmentioning
confidence: 99%
“…The empirical equation for coolant channels in pin-in block type fuels is used for the heat transfer coefficient and frication factor at the hot and cold channels (Kunitomi et al, 1991) (McEligot et al, 1965. The expression for natural convection between vertical parallel plates is used for the heat transfer coefficient at RPV outer surface (JSME, 1993).…”
Section: O Cmentioning
confidence: 99%