5. 5.25 Kg/s of oil with a relative density of 0.812 and a pressure of 311 kPa enters a short pipeline having an inlet diameter that is 1.5 times greater than outlet diameter. At the outlet the pressure is 295 kPa and is 2.25 m below the inlet. Neglecting friction and viscosity effects find the diameters of the inlet and outlet; and the velocities of the inlet and outlet pipes.
5. 5.25 Kg/s of oil with a relative density of 0.812 and a pressure of 311 kPa enters a short pipeline having an inlet diameter that is 1.5 times greater than outlet diameter. At the outlet the pressure is 295 kPa and is 2.25 m below the inlet. Neglecting friction and viscosity effects find the diameters of the inlet and outlet; and the velocities of the inlet and outlet pipes.
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
Transcribed Image Text:5. 5.25 Kg/s of oil with a relative density of 0.812 and a pressure of 311 kPa enters a short
pipeline having an inlet diameter that is 1.5 times greater than outlet diameter. At the outlet
the pressure is 295 kPa and is 2.25 m below the inlet. Neglecting friction and viscosity effects
find the diameters of the inlet and outlet; and the velocities of the inlet and outlet pipes.
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Follow-up Question
can you re work this.
I got 10.2 m/s for v2 and 4.54 m/s for v1
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