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Flow through the converging nozzle in Fig. P4.2 can be approximated by the one-dimensional velocity distribution u- Vo( 1 +4) v- 0 w 0 (a) Find a general expression for the fluid acceleration in the nozzle. (b) For the specific case Vo = 10 ft/s and L= 6 in, compute the acceleration, in g's, at the entrance and at the exit. Vo -u = 3V0 x=L P4.2

Flow through the converging nozzle in Fig. P4.2 can be approximated by the one-dimensional velocity distribution u- Vo( 1 +4) v- 0 w 0 (a) Find a general expression for the fluid acceleration in the nozzle. (b) For the specific case Vo = 10 ft/s and L= 6 in, compute the acceleration, in g's, at the entrance and at the exit. Vo -u = 3V0 x=L P4.2

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Flow through the converging nozzle in Fig. P4.2 can be approximated by the one-dimensional velocity distribution u- Vo( 1 +4) v- 0 w 0 (a) Find a general expression for the fluid acceleration in the nozzle. (b) For the specific case Vo = 10 ft/s and L= 6 in, compute the acceleration, in g's, at the entrance and at the exit. Vo -u = 3V0 x=L P4.2
Transcribed Image Text:Flow through the converging nozzle in Fig. P4.2 can be approximated by the one-dimensional velocity distribution u- Vo( 1 +4) v- 0 w 0 (a) Find a general expression for the fluid acceleration in the nozzle. (b) For the specific case Vo = 10 ft/s and L= 6 in, compute the acceleration, in g's, at the entrance and at the exit. Vo -u = 3V0 x=L P4.2
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