# Question - r/R)1/6 As shown in the figure below, an incompressible liquid of density p flows steadily and horizontally in a circular cross-sectional pipe. At section (1), the velocity profile over the cross-sectional area is uniform at Uo. At section (2), the flow is turbulent, and the velocity profile is u = Umax (1 –r where Umar is the centerline velocity in the axial z-direction, R is the pipe radius, and r is the radius from the pipe axis. The pressure at sections (1) and (2) are P1 = 52kPa (guage) and P2 = 50 kPa (gauge), respectively. Ignore the effects of gravity. Assume p= 1000 kg/m², R=1 cm and U = 5 m/s. Determine the magnitude of the wall frictional force D acting on the liquid between sections (1) and (2). D= 1 N. Section (1) (P1 Section (2) D ਡ VO u(r)

UFHS8F The Asker · Mechanical Engineering

Transcribed Image Text: - r/R)1/6 As shown in the figure below, an incompressible liquid of density p flows steadily and horizontally in a circular cross-sectional pipe. At section (1), the velocity profile over the cross-sectional area is uniform at Uo. At section (2), the flow is turbulent, and the velocity profile is u = Umax (1 –r where Umar is the centerline velocity in the axial z-direction, R is the pipe radius, and r is the radius from the pipe axis. The pressure at sections (1) and (2) are P1 = 52kPa (guage) and P2 = 50 kPa (gauge), respectively. Ignore the effects of gravity. Assume p= 1000 kg/m², R=1 cm and U = 5 m/s. Determine the magnitude of the wall frictional force D acting on the liquid between sections (1) and (2). D= 1 N. Section (1) (P1 Section (2) D ਡ VO u(r)
More
Transcribed Image Text: - r/R)1/6 As shown in the figure below, an incompressible liquid of density p flows steadily and horizontally in a circular cross-sectional pipe. At section (1), the velocity profile over the cross-sectional area is uniform at Uo. At section (2), the flow is turbulent, and the velocity profile is u = Umax (1 –r where Umar is the centerline velocity in the axial z-direction, R is the pipe radius, and r is the radius from the pipe axis. The pressure at sections (1) and (2) are P1 = 52kPa (guage) and P2 = 50 kPa (gauge), respectively. Ignore the effects of gravity. Assume p= 1000 kg/m², R=1 cm and U = 5 m/s. Determine the magnitude of the wall frictional force D acting on the liquid between sections (1) and (2). D= 1 N. Section (1) (P1 Section (2) D ਡ VO u(r)