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Mechanics of Fluids

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552 Compressible flow <strong>of</strong> gases<br />

throat and exit areas <strong>of</strong> the nozzle, the pressures in the reservoir<br />

and the nozzle throat and the temperature and velocity <strong>of</strong><br />

the air at exit.<br />

11.12 A convergent-divergent nozzle originally designed to give an<br />

exit Mach number <strong>of</strong> 1.8 with air is used with argon (γ = 5/3).<br />

What is the ratio <strong>of</strong> the entry stagnation pressure to the exit<br />

pressure when a normal shock is formed just inside the nozzle<br />

exit?<br />

11.13 The mass flow rate <strong>of</strong> superheated steam (γ = 1.3) is to be<br />

measured by a venturi-meter having inlet and throat diameters<br />

100 mm and 50 mm respectively. If the upstream stagnation<br />

pressure and stagnation temperature are respectively 200 kPa<br />

(absolute) and 150 ◦ C, what is the maximum mass flow rate<br />

that can be measured reliably in this way? Effects <strong>of</strong> friction<br />

and heat transfer may be neglected. (Thermodynamic tables<br />

will be needed.)<br />

11.14 Superheated steam from a large reservoir in which the pressure<br />

is 1 MPa flows adiabatically through a convergent-divergent<br />

nozzle for which the cross-sectional area at exit is twice that at<br />

the throat. The pressure beyond the exit is 700 kPa. Determine<br />

the Mach number <strong>of</strong> the flow in the exit plane, the crosssectional<br />

area at the plane where a normal shock may be<br />

expected in the nozzle, and the Mach number immediately<br />

upstream <strong>of</strong> the shock. What ambient pressure at exit would<br />

be necessary to produce isentropic supersonic flow without<br />

shocks? What exit pressure would give the same mass flow<br />

rate but with subsonic conditions throughout? Assume that<br />

frictional effects are negligible, that γ for superheated steam =<br />

1.3, and that the steam remains superheated and with constant<br />

specific heat capacities throughout. (Hint: From eqn 11.59<br />

substitute for m in eqn 11.60 to obtain p0 downstream <strong>of</strong> the<br />

shock.)<br />

11.15 Air flows adiabatically at the rate <strong>of</strong> 2.7 kg · s −1 through a<br />

horizontal 100 mm diameter pipe for which a mean value f =<br />

0.006 may be assumed. If the inlet pressure and temperature<br />

are 180 kPa and 50 ◦ C. What is the maximum length <strong>of</strong> the<br />

pipe for which choking will not occur? What are then the<br />

temperature and pressure at the exit end and half way along<br />

the pipe?<br />

11.16 Air enters a 150 mm diameter pipe (mean f = 0.006) at<br />

730 kPa and 30 ◦ C. For a flow rate <strong>of</strong> 2.3 kg · s −1 . What is the<br />

pressure 2 km from the inlet when the flow is (a) adiabatic,<br />

(b) isothermal?<br />

11.17 Calculate the diameter <strong>of</strong> a pipe 140 m long required to<br />

transmit air at 0.32 kg · s −1 under isothermal conditions if the<br />

inlet pressure and temperature are respectively 800 kPa and<br />

15 ◦ C and the pressure drop is not to exceed 200 kPa. Take<br />

f = 0.006.

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