How to find the velocity of a water leak in a spinning tank

In summary: It is a rotating liquid so Bernoulli is not applicable.In summary, we have a cylindrical water tank that spins over its axis of symmetry with constant angular velocity ω. To find the tangential and radial components of the velocity of the water as it leaves the tank, we can use the equations ##v_{r} = \sqrt{\frac{2P_{atm}}{\delta} - \omega^2 R^2}## and ##v_{t} = R \omega##, where ##P_{atm}## is atmospheric pressure, ##\delta## is the density of water, and ##R## is the radius of the tank. The time it takes the water to reach the floor is ##
  • #1
DigitalCrush
6
0
Homework Statement
Spinning water tank with a leak and constant angular speed
Relevant Equations
Bernoulli equation, constant acceleration kinematic equations, uniform circular motion equations.
We have a cylindrical water tank that spins over its axis of symmetry with constant angular velocity ω. Here's a diagram:

diagram.jpg


We wish to find:
1 - The tangential and radial components of the velocity of the water as it leaves the tank.
2 - The radius r reached by the water.

I'm not sure at all about how to handle the fact that the tank spins, as well as the deformation in the water surface. I chose to apply Bernoulli's equation and compare the point at the center of the surface, and the point where water leaves the tank:

##P_{atm} + \delta g_{ef} H = P_{atm} + \frac{1}{2} \delta v_{r}^2##. So: ##v_{r} = \sqrt{2Hg_{ef}}##

Where ##g_{ef} = g + a_{c} = g + R\omega ^2## is the effective acceleration of the water.

Then we have: ##v_{r} = \sqrt{2H(g + R \omega ^2)}##

The tangential component of the water's velocity is: ##v_{t} = R \omega##

The time it takes the water to reach the floor is ##t = \sqrt{\frac{2d}{g}}##, and ##r = R + v_{r}t##.

Thus: ##r = 2\sqrt{Hd(1 + \frac{R \omega ^2}{g})} + R##

My issue is that I have no idea if my ##g_{ef}## is correct. It seems to make sense because I expect ##r## and ##v_{r}## to be higher the larger ##ω## is. But I don't know how to explain why it makes sense to use it. That is, if it's even correct to begin with. I'm also not sure about using ##a_{c}=Rω^2## because I'm using the center point of the water surface, which is at ##r=0##.

Any help is appreciated. Thanks.
 
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  • #2
DigitalCrush said:
not sure at all about how to handle the fact that the tank spins
I couldn't follow your reasoning.
Suppose the difference in the height of the top surface between the centre and the edge is Y. I considered that:
- the pressure is constant across the exposed parabolic surface
- the surface profile is independent of the depth of liquid, so if we consider a surface within the drum the same as at the top surface (i.e., the top surface profle but replicated at some depth) the pressure will be constant across that.
- if we imagine the drum extended downwards, we can choose such a parabolic surface such that at the edge it touches the hole. The depth at its centre would be H+Y.
Is it reasonable to say that the pressure at that H+Y depth is ρg(H+Y)?
If so, that gives us the pressure at the hole.
 
  • #3
I think I understand most of your reasoning, but I'm not sure about how I could obtain Y in terms of the given data. Also, wouldn't the pressure at the hole be Patm, since it's exposed to the exterior of the tank?

Without obtaining Y in terms of the other quantities and assuming the pressure at the hole is ##\delta g (H+Y)##, I tried to get ##v_{r}##. By comparing the point at the center of the surface of the water and the hole (with height ##0## at the hole), I got:

##\delta g (H+Y) + \frac{1}{2} \delta v_{r}^2 = P_{atm} + \delta g H##

So ##v_{r} = \sqrt{\frac{2P_{atm}}{\delta} - 2gY}##

I'm not sure about this because I expect ##v_{r}## to be higher as ##\omega## increases, and I would expect ##Y## to also get larger as ##\omega## increases. By this formula, ##v_{r}## would actually be smaller as the tank spins faster.
 
Last edited:
  • #4
DigitalCrush said:
wouldn't the pressure at the hole be Patm, since it's exposed to the exterior of the tank?
The pressure just outside the hole is one atmosphere. To find the radial velocity of the jet you need the pressure difference from just inside. Compare with the equation with no rotation.
DigitalCrush said:
obtain Y in terms of the given data
I assumed you wouid know how to compute the surface of a rotating fluid.
Consider a small parcel of water on the surface at some radius x. Find an equation relating its tangential velocity to the slope of the surface and solve the differential equation.
 
  • #5
haruspex said:
Find an equation relating its tangential velocity to the slope of the surface and solve the differential equation.
Equivalently, consider the centrifugal force field. Integrate from x=0 to x=R to get the associated potential (the centrifugal pressure field). Add this to the pressure at the center of the bottom.
 
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  • #6
jbriggs444 said:
Equivalently, consider the centrifugal force field. Integrate from x=0 to x=R to get the associated potential (the centrifugal pressure field). Add this to the pressure at the center of the bottom.
Yes, that looks simpler.
 
  • #7
I found that ##Y = \frac{1}{2} \frac{\omega ^2}{g} R^2 ##. If the pressure at the hole is ## \delta g (H+Y) ##, then using Bernoulli's equation in the hole and the center of the water surface gives me: ## \delta g (H+Y) + \frac{1}{2} \delta v_{r}^2 = P_{atm} + \delta g H ##.

So ##v_{r} = \sqrt{\frac{2P_{atm}}{\delta} - 2gY} = \sqrt{\frac{2P_{atm}}{\delta} - \omega^2 R^2}##.

I expected that a larger ##\omega## would mean a larger ## v_{r} ##. Is this right?
 
  • #8
DigitalCrush said:
I found that ##Y = \frac{1}{2} \frac{\omega ^2}{g} R^2 ##. If the pressure at the hole is ## \delta g (H+Y) ##, then using Bernoulli's equation in the hole and the center of the water surface gives me: ## \delta g (H+Y) + \frac{1}{2} \delta v_{r}^2 = P_{atm} + \delta g H ##.

So ##v_{r} = \sqrt{\frac{2P_{atm}}{\delta} - 2gY} = \sqrt{\frac{2P_{atm}}{\delta} - \omega^2 R^2}##.

I expected that a larger ##\omega## would mean a larger ## v_{r} ##. Is this right?
A few things wrong there.
Atmospheric pressure applies both at the top of the liquid and just outside the hole, so cancels.
The excess pressure just inside the hole is is ## \delta g (H+Y) ##, but I do not understand how you obtained your "Bernoulli’s equation". You should take the radial velocity as zero just inside the hole and vr just outside.
 

1. How does the spinning of the tank affect the velocity of the water leak?

The spinning of the tank creates a centrifugal force, which can impact the velocity of the water leak. This force can either increase or decrease the velocity, depending on the direction of rotation and the location of the leak on the tank.

2. Can the velocity of the water leak be accurately measured while the tank is spinning?

Yes, the velocity of the water leak can be accurately measured using specialized equipment such as flow meters or pressure gauges. These instruments are designed to work in dynamic environments and can provide accurate readings even while the tank is spinning.

3. How does the size of the tank and the volume of water impact the velocity of the leak?

The size of the tank and the volume of water can affect the velocity of the leak in various ways. Generally, a larger tank with a higher volume of water will have a slower leak velocity due to the pressure being distributed over a larger area. However, the exact impact will also depend on the shape and design of the tank.

4. Is there a formula or equation to calculate the velocity of a water leak in a spinning tank?

Yes, there are various formulas and equations that can be used to calculate the velocity of a water leak in a spinning tank. These equations take into account factors such as the centrifugal force, pressure, and flow rate to determine the velocity of the leak. It is important to use the correct equation for the specific situation to ensure accurate results.

5. How can knowing the velocity of a water leak in a spinning tank be useful?

Knowing the velocity of a water leak in a spinning tank can be useful in many ways. It can help in identifying the location and severity of the leak, as well as determining the appropriate course of action to fix it. It can also provide valuable information for designing and improving tank systems to prevent future leaks.

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