A. 1.85
B. 0.1
C. 0.55
B. None of these
C. Shear stress
D. Shear force
A. 0.474
B. 4.728
D. 0.5
A. Flow is necessarily rotational
C. Radial component of velocity is same everywhere
D. Stream lines are not circular
A. Electromagnetic pump
C. Gear pump
D. Centrifugal pump
B. Multiplying with specific gravity
C. Dividing by specific gravity
D. Multiplying with density (gm/c.c)
B. Newtonian
C. Pseudo-plastic
D. Bingham plastic
A. Pressure gradient and rate of angular deformation
B. Shear stress and velocity
D. Velocity gradient and pressure intensity
B. Pseudo-plastic
C. Newtonian liquid
A. Sound to that of the fluid
B. Light to that of the fluid
C. Fluid to that of the light
A. Velocity of the fluid is very small
C. There is no entrainment of solids
D. The pressure drop is less than that for batch fluidisation
A. V2.7
B. V-0.2
C. V1.8
A. Remain same
B. Increases
D. May increase or decrease
B. Outer diameter only
C. Thickness only
D. Inner diameter
A. 1.5
C. 1
D. 2
A. Rate of transfer of molecular momentum
B. Cohesion
D. Neither A. nor B.
A. 5
C. 500
D. 5000
A. None of these
C. Friction factor
D. Dynamic pressure
B. 1.1
C. 60
D. 600
A. Viscous
C. Irrotational
D. Incompressible
A. 1 10-3 to 2 10-3 kg/m.s
B. 0.5 to 1 kg/m.s
D. 1 to 2 kg/m.s
A. Uniform, steady, incompressible, along a streamline
B. Steady, density being pressure dependent, frictionless
D. None of these
A. Temperature gradients are very high
B. Segregation of the solids occurs
C. Hot spots are formed
A. Geometrical similarity only
B. Dynamic similarity only
C. Both geometrical and dynamic similarity
A. (Q2 Q1)/Q1
B. Q2/Q1
D. Q1/Q2
A. Discharge of water by a centrifugal pump being run at a constant rpm
B. Water discharge from a vertical vessel in which constant level is maintained
C. Low velocity flow of a highly viscous liquid through a hydraulically smooth pipe
A. 0
D. > 1
B. 4.4
C. 44
D. 0.044
A. Rough and smooth pipes have the same friction factor
B. Laminar film covers the roughness projections
D. Friction factor depends upon NRe only
A. Formation of eddies within the stream
B. One in which dissipation of mechanical energy into heat occurs
D. Irrotational and frictional flow
A. Axial flow
C. None of these
D. Mixed flow
B. 147
C. 196
D. 49
A. 2.5
A. Unloads a pump
C. Provides back pressure for a cylinder
A. Rate of flow in each pipe is proportional to the length of
B. Head loss is same through
C. Total flow rate is the sum of flow rate in
A. 2 to 10
B. 0.1 to 2
D. 10 to 100
A. Hagen-Poiseuilles
B. Fannings
A. d2
C. d4
D. d
B. Independent of fluid density
D. Increases as fluid viscosity increases
A. Generally a needle valve
B. Helpful in easy removal of samples
C. Used to release any gases that might be vapour locking the pump
A. 32.36
B. 48.22
D. 7.65
A. Cohesion
B. Viscosity
C. Adhesion
A. Dependent on the buoyant forces only
B. Independent of the Metacentric height
D. Longer, if Metacentric height is increased
C. Prandtl mixing
D. Equivalent
B. Which needs a minimum shear, before it starts deforming
C. Which follows Newtons law of motion
A. Is constant over the entire cross-section
D. Is zero at the plates and increases linearly to the mid-plane
A. Dilatent
C. Bingham plastic
A. Flow-nozzle
B. ?p is same for all
C. Orificemeter
B. Four times as that of A
C. Same as that of A
D. Twice as that of A
B. 0.24
C. 24000
D. 24
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