Water at a gauge pressure of 3.8 atm at street level flows into an office building at a speed of 0.61 m/s through a pipe 5.5 cm in diameter. The pipe tapers down to 2.8 cm in diameter by the top floor, 18 m above, where the faucet has been left open. (Figure 1) Calculate the flow velocity in the pipe on the top floor. Assume no branch pipes and ignore viscosity. Express your answer using two significant figures. Figure Faucet 18 m P-3.8 atm 1 of 1 Ο ΑΣΦ Submit Request Answer Part B ? m/s Calculate the gauge pressure in the pipe on the top floor. Assume no branch pipes and ignore viscosity. Express your answer using two significant figures. P= Η ΑΣΦ Submit Request Answer Provide Feedback ? Pa

College Physics
11th Edition
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Chapter1: Units, Trigonometry. And Vectors
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Water at a gauge pressure of 3.8 atm at street level flows into an office
building at a speed of 0.61 m/s through a pipe 5.5 cm in diameter. The pipe
tapers down to 2.8 cm in diameter by the top floor, 18 m above, where the
faucet has been left open. (Figure 1)
Calculate the flow velocity in the pipe on the top floor. Assume no branch pipes and ignore viscosity.
Express your answer using two significant figures.
Figure
Faucet
18 m
P-3.8 atm
1 of 1
Ο ΑΣΦ
Submit
Request Answer
Part B
?
m/s
Calculate the gauge pressure in the pipe on the top floor. Assume no branch pipes and ignore viscosity.
Express your answer using two significant figures.
P=
Η ΑΣΦ
Submit
Request Answer
Provide Feedback
?
Pa
Transcribed Image Text:Water at a gauge pressure of 3.8 atm at street level flows into an office building at a speed of 0.61 m/s through a pipe 5.5 cm in diameter. The pipe tapers down to 2.8 cm in diameter by the top floor, 18 m above, where the faucet has been left open. (Figure 1) Calculate the flow velocity in the pipe on the top floor. Assume no branch pipes and ignore viscosity. Express your answer using two significant figures. Figure Faucet 18 m P-3.8 atm 1 of 1 Ο ΑΣΦ Submit Request Answer Part B ? m/s Calculate the gauge pressure in the pipe on the top floor. Assume no branch pipes and ignore viscosity. Express your answer using two significant figures. P= Η ΑΣΦ Submit Request Answer Provide Feedback ? Pa
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