What is the maximum speed of water flow in the intake pipe?

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Homework Help Overview

The discussion revolves around determining the maximum speed of water flow in an intake pipe connected to a pump located beneath a reservoir. The problem involves applying Bernoulli's principle in the context of fluid dynamics.

Discussion Character

  • Exploratory, Mathematical reasoning, Assumption checking

Approaches and Questions Raised

  • Participants are attempting to apply Bernoulli's equation to the scenario, discussing the relevant variables and constants. There is confusion regarding the application of pressure values and the treatment of certain terms in the equation.

Discussion Status

Some participants have provided guidance on which terms can be ignored and how to set up the equation. There is ongoing exploration of the correct application of Bernoulli's principle, with no explicit consensus reached yet.

Contextual Notes

Participants note the limited numerical information provided in the problem and question how to handle the assumptions regarding the speed of water at the surface and the pressure conditions.

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A pump and its horizontal intake pipe are located 11.5 m beneath the surface of a reservoir. The speed of the water in the intake pipe causes the pressure there to decrease, in accord with Bernoulli's principle. Assuming nonviscous flow, what is the maximum speed with which water can flow through the intake pipe?

--Im getting confused because they give you so few numbers to work with. Any ideas? Thanks, --

:smile:
 
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Bernoulli's Equation

[tex]P + \frac{1}{2} \rho v^2 + \rho gh = constant[/tex]

Well you know the density of the water and atmospheric pressure.
 
Ok so this is what I have: (P1) + ((1/2)density*v1^2) + (density*g*h1) = (P2) + ((1/2)density*v2^2) + (density*g*h2)

So for this question I can ignore the left side of this longer version of Bernoulli's? Do I substitute in a value of 1 or 0 so that I can solve for v ?
 
Ignore the speed of the water at the surface. (Assume the surface area is much greater than the cross-sectional area of the pipe.)
 
Ok am I on the right track with this? :

1.013 x 10^5 Pa = (1.013E5Pa + (1000 kg/m3*9.8m/s2*11.5m)) + .5(1000 kg/m3)* v^2 + (1000 kg/m3 *9.8m/s2 *11.5m)

Im trying to plug in what I know with Bernoulli's...
 
It should be:

[tex]P_{o} + \rho g h = P_{pipe} + \frac{1}{2} \rho v^2[/tex]
 
Last edited:

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