How Do You Calculate Reynolds Number for Flow Exiting a Rectangular Duct?

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SUMMARY

The discussion focuses on calculating the Reynolds Number for airflow exiting a rectangular duct, specifically using the formula Re = "rho"*V*d/"mu". Given parameters include air density ("rho") of 1.20 kg/m³, velocity (V) of 11 m/s, and viscosity ("mu") of 1.8418e-05 kg/m*s. The calculated Reynolds Number is 1.147e+05, based on an assumed diameter of 0.16 m derived from a symmetric flow model. The conversation highlights that once the fluid exits the duct, traditional pipe flow concepts, including the Moody diagram, become less applicable.

PREREQUISITES
  • Understanding of fluid dynamics principles
  • Familiarity with Reynolds Number calculations
  • Knowledge of airflow properties, including density and viscosity
  • Basic grasp of duct flow characteristics
NEXT STEPS
  • Research the implications of Reynolds Number in jet flow scenarios
  • Learn about the transition from laminar to turbulent flow in non-pipe systems
  • Explore alternative methods for characterizing flow after exiting ducts
  • Study the limitations of using Moody diagrams in various flow conditions
USEFUL FOR

Engineers, fluid dynamics researchers, and students studying airflow behavior in ducts and jets will benefit from this discussion.

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Homework Statement


Hi everyone,

This problem concerns calculating Reynold's Number of flow after exiting a duct. The duct that the flow exits is rectangular. The flow is measured directly underneath the center of the duct at a distance of 10 cm below the exit (Y-axis). Flow is measured at 11 m/s. It is determined that the velocity becomes 0 at a distance of 8 cm outward from the center (X axis). I am assuming that the flow is symmetric and thus the flow is esentially in a pipe with a radius of 8 cm.


Homework Equations



Re = "rho"*V*d/"mu"

The Attempt at a Solution



"rho" = density = 1.20 kg/m^3
V = velocity of air = 11 m/s
d = diameter of pipe = 2*0.08m = 0.16 m
"mu" = viscosity of air = 1.8418e-05 kg/m*s

plugging those into the equation above yields: Re=1.147e+05

I guess my question is regarding my assumtion of the pipe. Was I correct in my assumption?
 
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After the fluid leaves the pipe, the concept of a Reynolds number is kind of meaningless. Furthermore, the number can be based upon anything. Sure, pipe flow Reynolds numbers based on diameter are well known and can be a sure-fire way to indicate laminar vs turbulence. However, once the fluid leaves the pipe, you no longer have simple pipe flow. You now have a jet, and the concepts of walls and such no longer apply.

You certainly can measure the velocity and viscosity. After that, the characteristic length can be whatever you want it to be, there is no wrong answer. Having said that, you can also no longer use the pipe flow Moody diagram and so on and so forth.
 

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