Laminar forced convection in the entrance region of helical pipes
β Scribed by C.X. Lin; P. Zhang; M.A. Ebadian
- Publisher
- Elsevier Science
- Year
- 1997
- Tongue
- English
- Weight
- 988 KB
- Volume
- 40
- Category
- Article
- ISSN
- 0017-9310
No coin nor oath required. For personal study only.
β¦ Synopsis
In the present study, three-dimensional laminar forced flow and heat transfer in the entrance region of helical pipes have been investigated using a fully elliptic numerical method. Laminar flow and heat transfer were assumed to develop from the inlet to the outlet simultaneously. The governing equations were solved by means of a control-volume fiuite element method. The results presented in this paper cover a Reynolds munber range of 25G2000, a pitch range of O&0.6, and a curvature ratio range of 0.025-0.20. The present elliptic numerical results are compared with previous experimental data and parabolic numerical data. The developments of temperature field, main and secondary velocity fields, local and average friction factqrs, and local and average Nusselt numbers are given and discussed. It has been found that both the friction factor and Nusselt number are oscillatory in the entrance region of helical pipes. The pitch and Reynolds number exert different effects on the developments of the friction factor and Nusselt number than the curvature ratio.
π SIMILAR VOLUMES
The laminar flow of all illcompressible fluid in the inlet of a pipe is allalyzed llumerically. The numerical technique allows a closer approximatioll to the basic equatiolls of fluid motioll than has been possible in previous illvestigations. Significallt differellces are showll betweell the result
The transient heat transfer problem referring to a fully laminar flow developing in pipes exposed to a step change in the temperature is studied here. Bi-dimensional (axial-radial) wall and fluid heat conduction are assumed. The effects of pipe thickness, PΓ©clet number, wallto-fluid conductivity rat