a. 0.03 ![]() |
||
b. 0.3 ![]() |
||
c. 5 ![]() |
||
d. 1 ![]() |
a. 2,300-4,000 ![]() |
||
b. 500-1,000 ![]() |
||
c. 105 -106 ![]() |
||
d. 50,000-100,000 ![]() |
a. The friction factor decreases. ![]() |
||
b. The friction factor is kept constant. ![]() |
||
c. The friction factor increases. ![]() |
||
d. None of the above ![]() |
a. M L-1 ![]() |
||
b. M L-1T-2 ![]() |
||
c. M2L-1T ![]() |
||
d. M-1T-2 ![]() |
a. Thermal conductivity ![]() |
||
b. Wind velocity ![]() |
||
c. Atmospheric pressure ![]() |
||
d. Relative humidity ![]() |
a. The ratio of inertial forces to viscous forces. ![]() |
||
b. The ratio of surface tension to inertial forces. ![]() |
||
c. The ratio of inertial forces to gravitational forces. ![]() |
||
d. The ratio of momentum diffusivity to thermal diffusivity. ![]() |
a. The ratio of inertial forces ρV2/L to viscous forces μV/L2 ![]() |
||
b. The ratio of surface tension to inertial forces ![]() |
||
c. The ratio of gravitational force to fluid’s inertia ![]() |
||
d. The ratio of momentum diffusivity to thermal diffusivity ![]() |
a. Movement of fluid slowly in layers in a pipe, without much mixing among the layers ![]() |
||
b. A flow whose Reynolds number exceeds 2300 ![]() |
||
c. Movements of fluid are chaotic with significant mixing ![]() |
||
d. None of the above ![]() |
a. Pressure is the force divided by the area over which the force is applied. ![]() |
||
b. Pressure is equal to surface tension. ![]() |
||
c. Pressure is the force times the area over which the force is applied. ![]() |
||
d. Pressure is equal to the object’s acceleration times its mass. ![]() |
a. Reynolds number ![]() |
||
b. Weber number ![]() |
||
c. Prandtl number ![]() |
||
d. Froude number ![]() |
a. The locus of points of all the fluid particles that have passed through a given point ![]() |
||
b. A family of curves, which are normal to the velocity vector of the flow ![]() |
||
c. A family of curves that track the trajectories of fluid particles ![]() |
||
d. A family of curves that are instantaneously tangent to the velocity vector of the flow ![]() |
a. Pressure coefficient ![]() |
||
b. Mach number M ![]() |
||
c. Gas constant R ![]() |
||
d. Friction factor f ![]() |
a. V2/Lg ![]() |
||
b. µ VL/ρ ![]() |
||
c. VL/σ ![]() |
||
d. None of the above ![]() |
a. Streamlines cannot cross each other. ![]() |
||
b. Streamlines provide a snapshot of the entire flow field. ![]() |
||
c. Streamlines track trajectories of fluid particles. ![]() |
||
d. The tangent at each point on a streamline is the direction of the velocity vector at that point. ![]() |
a. The streamwise velocity component satisfies uz = 0. ![]() |
||
b. “Boundary layers” from opposite sides of the pipe are separated and continue growing. ![]() |
||
c. The radial component of the velocity is zero. ![]() |
||
d. The entrance length depends on the Reynolds number. ![]() |
a. Surface tension is responsible for the weight of liquid droplets. ![]() |
||
b. Surface tension is measured in forces per unit length or of energy per unit area. ![]() |
||
c. Surface tension is responsible for buoyancy. ![]() |
||
d. None of the above ![]() |
a. In the laminar zone, friction factor decreases as the Reynolds number increases. ![]() |
||
b. In the turbulent zone, friction factor increases as the relative roughness (D/ε) increases. ![]() |
||
c. Within the zone of complete turbulence, friction factor is independent of Reynolds number. ![]() |
||
d. As relative roughness increases, the boundary of the complete turbulence zone shifts to the right. ![]() |
a. Viscosity of a fluid depends strongly on its temperature. ![]() |
||
b. Viscosity measures the friction between the fluid and the wall. ![]() |
||
c. Shear stress is independent of viscosity. ![]() |
||
d. For a given rate of angular deformation of a fluid, shear stress is inversely proportional to viscosity. ![]() |
a. 15.7 kPa ![]() |
||
b. 25.3 kPa ![]() |
||
c. 3.21 kPa ![]() |
||
d. 1.24 kPa ![]() |
a. 1 m ![]() |
||
b. 60 cm ![]() |
||
c. 6 m ![]() |
||
d. 20 cm ![]() |
a. 331.3 m/s ![]() |
||
b. 13.2 m/s ![]() |
||
c. 1520.2 m/s ![]() |
||
d. 212.5 m/s ![]() |
a. 1.14 108 lbf ![]() |
||
b. 4.14 108 lbf ![]() |
||
c. 6.14 108 lbf ![]() |
||
d. 9.14 108 lbf ![]() |
a. 0.06 m3/s ![]() |
||
b. 1.2 m3/s ![]() |
||
c. 0.01 m3/s ![]() |
||
d. 0.12 cm3/s ![]() |
a. 3 ![]() |
||
b. 5 ![]() |
||
c. 12 ![]() |
||
d. -2 ![]() |
a. a = b ![]() |
||
b. a = 2b ![]() |
||
c. a = -b ![]() |
||
d. a = -2b ![]() |
a. -3 ![]() |
||
b. 2 ![]() |
||
c. 32 ![]() |
||
d. -8 ![]() |
a. Supersonic ![]() |
||
b. Both turbulent and laminar ![]() |
||
c. Turbulent ![]() |
||
d. Laminar ![]() |
a. 1.55 10-4 m2/s ![]() |
||
b. 1.25 10-4 m2/s ![]() |
||
c. 0.5 10-4 m2/s ![]() |
||
d. 1.55 10-6 m2/s ![]() |
a. 367 N/m2 ![]() |
||
b. 65 N/m2 ![]() |
||
c. 550 N/m2 ![]() |
||
d. 107 N/m2 ![]() |
a. 100 m/s ![]() |
||
b. 400 m/s ![]() |
||
c. 200 m/s ![]() |
||
d. 50 m/s ![]() |
a. 15 m ![]() |
||
b. 50 m ![]() |
||
c. 12 m ![]() |
||
d. 8 m ![]() |
a. 11 µ ![]() |
||
b. 0 ![]() |
||
c. µ ![]() |
||
d. 2 µ ![]() |
a. 62 µ ![]() |
||
b. 0 ![]() |
||
c. 22µ ![]() |
||
d. 38 µ ![]() |
a. µ ![]() |
||
b. 10µ ![]() |
||
c. 20πµ ![]() |
||
d. 10πµ ![]() |
a. 0.5 g ![]() |
||
b. 2.6 g ![]() |
||
c. 5.2 g ![]() |
||
d. 7.9 g ![]() |
a. 10 s ![]() |
||
b. 12 s ![]() |
||
c. 7 s ![]() |
||
d. 20 s ![]() |
a. 1.26 N ![]() |
||
b. 5.23 N ![]() |
||
c. 2.12 N ![]() |
||
d. 0.12 N ![]() |
a. 5 m/s ![]() |
||
b. 1 m/s ![]() |
||
c. 2 m/s ![]() |
||
d. 0.5 m/s ![]() |
a. 31.1 kN ![]() |
||
b. 27.2 kN ![]() |
||
c. 19.6 kN ![]() |
||
d. 59.5 kN ![]() |
a. 7.6 mm ![]() |
||
b. 5.3 mm ![]() |
||
c. 1.2 mm ![]() |
||
d. 8.7 mm ![]() |
a. 0.15 psi ![]() |
||
b. 1.24 psi ![]() |
||
c. 16.3 psi ![]() |
||
d. 350 psi ![]() |
a. 1.2 l/s ![]() |
||
b. 3.9 l/s ![]() |
||
c. 45.1 l/s ![]() |
||
d. 0.2 l/s ![]() |
a. 0.0004 ![]() |
||
b. 0.004 ![]() |
||
c. 0.04 ![]() |
||
d. 0.4 ![]() |
a. 119 Pa/m ![]() |
||
b. 1049 Pa/m ![]() |
||
c. 22 Pa/m ![]() |
||
d. 11 Pa/m ![]() |
a. 5.3 mPa s ![]() |
||
b. 0.005 cP ![]() |
||
c. 5.3 Pa s ![]() |
||
d. 5.3 P ![]() |
a. 0.3 atm ![]() |
||
b. 0.03 atm ![]() |
||
c. 3 Pa ![]() |
||
d. 30 Pa ![]() |
a. Mf D v/μ ![]() |
||
b. Mf/(D μ) ![]() |
||
c. Mf v ρ/μ ![]() |
||
d. Mf ρ D/μ ![]() |
a. 1.22 ![]() |
||
b. 2.0 ![]() |
||
c. 0.52 ![]() |
||
d. 7 ![]() |
a. 1 ![]() |
||
b. 2 ![]() |
||
c. 1.5 ![]() |
||
d. 5 ![]() |
a. dP/dz ![]() |
||
b. 2 π R dP/dz ![]() |
||
c. μ dP/dz ![]() |
||
d. R2π dP/dz ![]() |
a. 225 atm ![]() |
||
b. 0.225 atm ![]() |
||
c. 2250 Pa ![]() |
||
d. 225 Pa ![]() |
a. 0.2 Pa s ![]() |
||
b. 1 cP ![]() |
||
c. 0.2 cP ![]() |
||
d. 1 Pa s ![]() |
a. 112 ![]() |
||
b. 225 ![]() |
||
c. 325 ![]() |
||
d. 176 ![]() |
a. 40 ![]() |
||
b. 33 ![]() |
||
c. 32 ![]() |
||
d. 35 ![]() |
a. 280, 10 ![]() |
||
b. 210, 10 ![]() |
||
c. 280, 20 ![]() |
||
d. 210, 20 ![]() |