The continuity equation and Navier-Stokes equations derived from a non-orthogonal helical coordinate system are solved by the Galerkin finite-element method in an attempt to study the torsion effect on the fully developed laminar flow in the helical square duct. Since high-order terms of curvature and torsion are considered, the approach is also applicable to the problems with finite curvature and torsion. The interaction effects of curvature, torsion, and the inclined angle of the cross section on the secondary flow, axial velocity, and friction factor in the helical square duct are presented. The results show that the torsion has more pronounced effect on the secondary flow rather than the axial flow. In addition, unlike the flow in the toroidal square duct, Dean’s instability of the secondary flow, which occurs near the outer wall in the helical square duct, can be avoided due to the effects of torsion and/or inclined angle. In such cases, a decrease of the friction factor is observed. However, as the pressure gradient decreases to a small value, the friction factor for the toroidal square duct is also applicable to the helical square duct.
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June 1993
Research Papers
The Torsion Effect on Fully Developed Laminar Flow in Helical Square Ducts
Wen-Hwa Chen,
Wen-Hwa Chen
Department of Power Mechanical Engineering, National Tsing Hua University, Hsinchu, Taiwan 30043
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Ray Jan
Ray Jan
Department of Power Mechanical Engineering, National Tsing Hua University, Hsinchu, Taiwan 30043
Search for other works by this author on:
Wen-Hwa Chen
Department of Power Mechanical Engineering, National Tsing Hua University, Hsinchu, Taiwan 30043
Ray Jan
Department of Power Mechanical Engineering, National Tsing Hua University, Hsinchu, Taiwan 30043
J. Fluids Eng. Jun 1993, 115(2): 292-301 (10 pages)
Published Online: June 1, 1993
Article history
Received:
December 17, 1991
Revised:
March 3, 1993
Online:
May 23, 2008
Citation
Chen, W., and Jan, R. (June 1, 1993). "The Torsion Effect on Fully Developed Laminar Flow in Helical Square Ducts." ASME. J. Fluids Eng. June 1993; 115(2): 292–301. https://doi.org/10.1115/1.2910138
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