I Mathematical Procedure for Obtaining Velocity Profile in Laminar Flow

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The discussion focuses on deriving the velocity profile for laminar flow in a round pipe using a force balance approach. Participants clarify the correct formulation of shear stress and pressure terms in the governing equations. The integration process for the velocity gradient is debated, with emphasis on boundary conditions and constants of integration. The correct expression for velocity is established, incorporating the non-slip condition at the pipe wall. Overall, the conversation highlights the mathematical steps necessary to accurately model laminar flow in a cylindrical geometry.
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Hi guys,
i'm trying to find the velocity profile for a laminar flow in a round pipe.
Starting from a force balance, we can obtain the first equation high in the left. I started with a procedure but i think I'm making mistakes.
Can you suggest me the mathematical procedure?
 

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Andrea Vironda said:
Hi guys,
i'm trying to find the velocity profile for a laminar flow in a round pipe.
Starting from a force balance, we can obtain the first equation high in the left. I started with a procedure but i think I'm making mistakes.
Can you suggest me the mathematical procedure?

Shouldn't the force balance look like this:

$$\underbrace{-\mu\frac{du}{dr}}_{\tau}\underbrace{2\pi r}_{P} = \frac{\partial p}{\partial x} \underbrace{\pi r^2}_{A}$$

- no gravity
- no acceleration
- no viscous normal stresses
 
Hi,
i considered a ring-shaped volume element, so $$(2\pi r dr P)_{x}-(2\pi r dr P)_{x+dx}+(2\pi r dr \tau)_{r}-(2\pi r dr \tau)_{r+dr}=0$$ I divided by ##2\pi r dr dx## and took the limit ##dr, dx \to 0##
 
Andrea Vironda said:
Hi,
i considered a ring-shaped volume element, so $$(2\pi r dr P)_{x}-(2\pi r dr P)_{x+dx}+(2\pi r dr \tau)_{r}-(2\pi r dr \tau)_{r+dr}=0$$ I divided by ##2\pi r dr dx## and took the limit ##dr, dx \to 0##

I don't understand your 3rd and 4th term, I would have written them as

$$(2\pi r dx \tau)_{r}-(2\pi r dx \tau)_{r+dr}=0$$

since the shear stresses act on the surface of the sleeve, not on the front and back.
 
Last edited:
Andrea Vironda said:
Hi guys,
i'm trying to find the velocity profile for a laminar flow in a round pipe.
Starting from a force balance, we can obtain the first equation high in the left. I started with a procedure but i think I'm making mistakes.
Can you suggest me the mathematical procedure?
Your 2nd integration was done incorrectly. First you solve for du/dr:
$$\frac{du}{dr}=\frac{r}{2\mu}\frac{dp}{dx}+\frac{C_1}{r}$$du/dr is zero at r = 0 so ##C_1=0##. So you now have:
$$\frac{du}{dr}=\frac{r}{2\mu}\frac{dp}{dx}$$
What do you get when you integrate that, subject to the boundary condition u = 0 at r = R?
 
stockzahn said:
I don't understand your 3rd and 4th term, I would have written them as

$$(2\pi r dx \tau)_{r}-(2\pi r dx \tau)_{r+dr}=0$$

since the shear stresses act on the surface of the sleeve, not on the front and back.
Yup, you're right

Chestermiller said:
Your 2nd integration was done incorrectly. First you solve for du/dr:
$$\frac{du}{dr}=\frac{r}{2\mu}\frac{dp}{dx}+\frac{C_1}{r}$$du/dr is zero at r = 0 so ##C_1=0##. So you now have:
$$\frac{du}{dr}=\frac{r}{2\mu}\frac{dp}{dx}$$
What do you get when you integrate that, subject to the boundary condition u = 0 at r = R?

I obtain $$\Delta u=\frac{r^2}{2}\frac{1}{2\mu}\frac{dP}{dx}+C_2$$ how can i arrange accourding to boundary conditions? is ##\Delta u=u(R)-u(0)##?
 
Last edited:
Andrea Vironda said:
Yup, you're right
I obtain $$\Delta u=\frac{r^2}{2}\frac{1}{2\mu}\frac{dP}{dx}+C_2$$ how can i arrange accourding to boundary conditions? is ##\Delta u=u(r)-u(0)##?
When you have a constant of integration, there is no need to write ##\Delta u##. You simply can write u:
$$u=\frac{r^2}{2}\frac{1}{2\mu}\frac{dP}{dx}+C_2$$To determine the constant of integration ##C_2##, you simply make use of the non-slip boundary condition at the wall u(R)=0, where R is the radius of the tube.
 
Chestermiller said:
When you have a constant of integration, there is no need to write ##\Delta u##. You simply can write u
Ok the procedure is clear, but why i shouldn't write as ##\Delta u##?
 
Andrea Vironda said:
Ok the procedure is clear, but why i shouldn't write as ##\Delta u##?
Because you didn't use a ##\Delta r## on the other side of the equation. I guess what you did is OK if you say (as you suggested) that ##\Delta u=u(r)-u(0)##, but then you could have moved u(0) over to the other side of the equation and absorbed it into ##C_2##.
 
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