Air flows adiabatically between two sections in a constant area pipe. At upstream section \((1), p_{0,1}=100\) psia, \(T_{0,1}=600^{\circ} \mathrm{R}\) and \(\mathrm{Ma}_{1}=0.5 .\) At downstream section \((2),\) the flow is choked. Estimate the magnitude of the force per anit cross-sectional area exerted by the inside wall of the pipe on the fluid between sections (1) and (2).

Short Answer

Expert verified
The force per unit cross-sectional area exerted by the inside wall of the pipe on the fluid is the difference in pressures at the upstream and downstream, calculated by using adiabatic and isentropic flow relationships.

Step by step solution

01

Assume the conditions for choked flow and Adiabatic flow

When considering an adiabatic process with negligible shaft work, choked flow occurs when the Mach number \(Ma = 1\). Therefore, it can be assumed that at downstream section (2), \(\mathrm{Ma}_{2}=1\). Also, the given ambient conditions at the upstream are, \(p_{0,1}=100\) psia and \(T_{0,1}=600^{\circ} R\)
02

Calculate the ideal gas constant

The ideal gas constant (R) can be obtained if we assume that the working fluid is air, which is a diatomic molecule. Thus, air can be seen as calorically perfect and the ideal gas constant for air is \(R = 53.3 \, lb_f \cdot ft / (lb_m \cdot ^{\circ}R)\).
03

Apply the isentropic flow relationships

Isentropic flow relations can be used to calculate the pressure and temperature at the downstream (2) from the given conditions at the upstream flow. For a calorically perfect gas undergoing an isentropic process, the following relationships give the static to stagnation conditions: \(T_1/T_{0,1} = 1 + ((\gamma - 1)/2) * Ma_1^2\) and \(T_2/T_{0,2} = 1 + ((\gamma - 1)/2) * Ma_2^2\), where \(\gamma=1.4\) is the specific heat ratio for a calorically perfect gas. Solving these for \(T_1\) and \(T_2\), we get the temperatures at upstream and downstream.
04

Evaluate the temperature ratio

With these temperatures \(T_1\) and \(T_2\) obtained, the ratio \(T_{0,2} / T_{0,1}\) can be evaluated.
05

Calculate the static pressure at downstream

Applying the isentropic flow relations again, this time to obtain pressure relations at the upstream and downstream - the static pressures can be obtained. They can be calculated as \(p_1/p_{0,1}= \left[1 + ((\gamma - 1)/2) * Ma_1^2\right]^{\frac{-\gamma}{\gamma -1}}\) and \(p_2/p_{0,2}= \left[1 + ((\gamma - 1)/2) * Ma_2^2\right]^{\frac{-\gamma}{\gamma -1}}\). From these, we can compute the pressures \(p_1\) and \(p_2\).
06

Estimate the magnitude of the force

The force exerted by the inside wall of the pipe on the fluid is related to the change in momentum of the fluid due to the change in pressure between sections 1 and 2. It can be written as \(F/A = p_1 - p_2\), where A is the constant cross-sectional area of the pipe. Knowing \(p_1\) and \(p_2\), the force can be estimated.

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Most popular questions from this chapter

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