CFD Simulation Projects by ANSYS Fluent

CFD Simulation Projects by ANSYS Fluent

47
14h 42m 35s
  1. Section 1

    Forced Convection

  2. Section 2

    Moving Reference Frame (MRF)

  3. Section 3

    Gas & Petrochemical

  4. Section 4

    Aerodynamics & Aerospace

    1. Episode 7 1h 3m 43s Free
  5. Section 5

    Mechanical

  6. Section 6

    HVAC

  7. Section 7

    Chemical

  8. Section 8

    Architectural

  9. Section 9

    Hydraulic Structure & Civil

  10. Section 10

    Multi-Phase Flow

  11. Section 11

    Porous

MR CFD
Oops! You are not logged in.

For watching this episode you should sign in first, if you don't have an account, you can create one in seconds.

Toggle Episode List

CFD Simulation Projects by ANSYS Fluent — Ep 07

Laminar Flow Heat Transfer in U-Bend, Paper Validation. CFD approach

Episode
07
Run Time
17m 51s
Published
Apr 05, 2025
Course Progress
0%
Mark as Complete
Add to Watchlist
About This Episode

Overview of CFD Simulation of Laminar Flow and Heat Transfer in a U-Bend

Project Description

Validated against the paper "Laminar flow and heat transfer in U-bends: The effect of secondary flows in ducts with partial and full curvature," this ANSYS Fluent simulation models laminar flow through a U-shaped tube.

Model Design

The fluid, therminol, has particular characteristics: density of 793.9 kg/m³, specific heat capacity of 2315 J/kg·K, thermal conductivity of 0.116 W/m·K, and viscosity of 0.00173 kg/m·s.  With an inlet speed of 0.21791 m/s, the simulation runs at a Reynolds number of 1000.  Designed in Design Modeller, the U-bend model has a pipe diameter of 0.01 m and a bend radius of 0.015 m.  There are 2,268,000 components in the structured mesh.

Methodology

A constant heat flux of 1156 W/m²·K is applied as the thermal boundary condition on the pipe wall to analyze fluid behavior and heat transfer through the U-bend.

Results and Conclusion

Validated against Figure 14-b of the reference paper, the simulation seeks to confirm fluid temperature variations along the inner wall of the pipe.  A graph of dimensionless position versus dimensionless temperature backs this confirmation.  The Nusselt number is also evaluated at P1 to P5 along the bend; ratios are computed in relation to section P1.  These results are contrasted with dimensionless Nusselt numbers in Figure 19-b of the paper.

Download Geometry And Mesh Files