Turbulent flow velocity profiles

In summary, the conversation discusses how to plot velocity profiles for turbulent flow in different duct and pipe sizes. It provides equations and steps for calculating mean velocity, average velocity at the centre line, and the values for f and ΔP/L. The conversation also mentions using the Blasius equation and the Reynolds number to calculate these values.
  • #1
suvernfraggle
3
0
i've been given this question by my lecturer at university and I am struggling with where to start with it to be honest. it feels like i don't have enough information. please can someone help?

For turbulent flow, the velocity profile inside a duct and a pipe of diameters Dd and Dp and
both with distance y from the centre line is: vy/vy=0 = (1-y/r)1/7, where vy=0 = vmean/0.817 and vmean=Q/A. Plot the velocity profiles for:

(a) Air flowing in a duct measuring Dd = 0.6m and with Re = 105.
(b) Water flowing in a pipe measuring Dp = 0.5m and with Re = 105.
(c) Calculate the vmean and vy=0 for both cases (a) and (b)
(d) If the Blasius equation f = 0.079Re-0.25 applies, calculate the values of f and ΔP/L for (a)
 
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  • #2
and (b).To answer this question, you will need to start by calculating the mean velocity (vmean) for each case (a) and (b). This can be done using the equation given: vmean = Q/A, where Q is the volumetric flow rate (in m3/s) and A is the cross-sectional area of the duct or pipe (in m2). Once you have calculated vmean, you can then calculate vy=0 (the average velocity at the centre line) using the equation: vy=0 = vmean/0.817.Next, you will need to plot the velocity profiles for both cases (a) and (b). To do this, you will need to calculate the value of 'r' (the radius of the duct or pipe) for each case. Then, using the equation vy/vy=0 = (1-y/r)1/7, you can calculate the values of vy/vy=0 for different distances y from the centre line (i.e. 0, 0.1, 0.2 etc.). These values can then be plotted on a graph against y to give the velocity profile for each case.Finally, to calculate the values of f and ΔP/L for each case, you will need to use the Blasius equation f = 0.079Re-0.25. Here, Re is the Reynolds number for each case (which you should already have calculated), and f is the friction factor. The value of ΔP/L can then be calculated using the equation ΔP/L = 4fLvmean2/D, where L is the length of the duct or pipe (in m), and D is the diameter of the pipe or duct (in m).
 

FAQ: Turbulent flow velocity profiles

What is turbulent flow velocity profile?

Turbulent flow velocity profile refers to the variation of fluid velocity across a cross-section of a pipe or channel in turbulent flow. It is influenced by factors such as fluid viscosity, flow rate, and surface roughness.

How is turbulent flow velocity profile different from laminar flow velocity profile?

In a laminar flow, the velocity profile is parabolic, with the maximum velocity at the center of the pipe or channel. In contrast, the velocity profile in a turbulent flow is flattened and irregular, with higher velocities near the walls and lower velocities in the center.

What is the significance of turbulent flow velocity profile?

The turbulent flow velocity profile is important in understanding the behavior of fluids in turbulent flow, which is commonly encountered in many industrial and natural processes. It affects the transport of particles and heat, as well as the overall efficiency of fluid systems.

How is turbulent flow velocity profile measured?

There are various methods for measuring turbulent flow velocity profiles, such as hot-wire anemometry, laser Doppler anemometry, and particle image velocimetry. These techniques use different principles to measure the velocity of fluid particles at different locations within the flow.

Can the turbulent flow velocity profile be predicted?

While it is difficult to predict the exact turbulent flow velocity profile, there are mathematical models and equations that can estimate the average velocity profile based on parameters such as Reynolds number and turbulence intensity. However, these predictions may not be accurate for complex flows with varying conditions.

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