๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Developing turbulent convective heat transfer in helical pipes

โœ Scribed by C.X. Lin; M.A. Ebadian


Publisher
Elsevier Science
Year
1997
Tongue
English
Weight
1023 KB
Volume
40
Category
Article
ISSN
0017-9310

No coin nor oath required. For personal study only.

โœฆ Synopsis


A fully elliptic numerical study has been carried out to investigate three-dimensional turbulent developing convective heat transfer in helical pipes with finite pitches. The k-e standard two-equation turbulence model is used to simulate turbulent flow. The governing equations are solved by a controlvolume finite element method. Numerical results have been compared to the existing experimental data and a good agreement has been obtained. The results presented in this paper cover a Reynolds number range of 2.5 x lo4 N 1.0 x lo', a pitch range of 0.0 _ 0.6 and a curvature ratio range of 0.025 _ 0.050. The developments of effective thermal conductivity and temperature fields and local and average Nusselt numbers are given and discussed. It has been found that the examined parameters exert complex effects on developing thermal fields and heat transfer in the helical pipes. The Nusselt numbers for the helical pipes are oscillatsory before the flow is fully developed, especially for the case of relatively large curvature ratio.


๐Ÿ“œ SIMILAR VOLUMES


Theoretical and numerical analysis of co
โœ Huajun Chen; Benzhao Zhang; Jianfeng Ma ๐Ÿ“‚ Article ๐Ÿ“… 2003 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 407 KB

In terms of the tensor analysis technique, the relative N-S equations and the energy equation in a rotating helical coordinate system are presented in this paper. Convective heat transfer in the rotating helical pipes with circular crosssection is investigated employing theoretical and numerical met

Turbulent convective transfer in plate h
โœ W.W Focke ๐Ÿ“‚ Article ๐Ÿ“… 1983 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 345 KB

Readily available data on turbulent transfer in plate heat exchangers can be correlated by a heat transfer-energy dissipation analogy: N~ 3 e g,~Pr,Vi) = C 3(fRe ) in which the Nusselt number modified for changes in the Prandtl number and bulk to wall viscosity ratio Vi is related to the friction fa

Heat transfer in turbulent pipe flow
โœ Raul R. Hunziker ๐Ÿ“‚ Article ๐Ÿ“… 1958 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 945 KB

Heat transfer to and from fully developed turbulent flow in a circular pipe and between parallel plates is analyzed. The use of Pal's velocity and correlation distributions allows a consistent determination of the eddy diffusivity for heat \*u = a\*u. The average of this \*x distribution across th