A. 3y/4
B. 1/(y/4)
D. 1/(y/3)
A. Flow in an open channel
B. A disturbance travelling upstream in moving fluid
D. None of these
A. Gravity
B. Viscous
A. Linear
B. Hyperbolic
D. Logarithmic
A. 0.1
B. 0.01
C. 0.3
A. 5
B. 100
D. 50
A. None of these
C. Fluid on the solid in a direction opposite to flow
D. Solid on the fluid
A. Pitot tube
B. Segmental orificemeter
D. Rotameter
A. Decreasing the size of the inlet pipe
B. Increasing the size of the inlet pipe
C. Lowering the pump position
A. 10
C. 2000
D. 100
B. < 5
C. > 1
A. 20 and 120
B. 45 and 60
D. 90 and 80
B. gm/cm2. sec
C. cm2/sec
D. m2/sec
A. 1/?
B. 1/?2
D. ?2
B. Blake-Plummer equation
C. Fanning equation
D. Hagen-Poiseuille equation
A. Outlet tip of a blade curves in a direction opposite to that
B. Inlet tip of a blade curves in a direction opposite to that
D. Inlet tip of a blade is towards the direction
B. Root mean square of velocity fluctuations in the three co-ordinate directions
C. Temporal velocity components
C. Slurries
D. Viscous mass
A. Increase
B. Remain same
D. Unpredictable
A. I, II, III
C. I, II, V
D. II, IV, V
A. 10 psi, 19.7 ft. of water, 5.3 inches of Hg
B. 10 psi, 19.7 ft. of water, 23.3 inches of Hg
C. 4.33 psi, 10 ft. of water, 20.7 inches of Hg
A. Reciprocating compressor
C. Centrifugal compressor
D. Axial flow compressor
A. Orificemeter
C. Venturimeter
D. Flow nozzle
A. As the square of the radius
B. Linearly as the viscosity
D. Inversely as the pressure drop
A. Increases due to increased vapour pressure
B. Decreases due to reduced viscosity
C. Decreases due to increased frictional resistance
A. Decreases in the downstream direction
C. Is independent of the area of flow
D. Is constant
B. Velocity
C. None of these
D. Turbulence
A. Gate valve
B. Check valve
D. Butterfly valve
A. al to 50 D
C. 5. D.NRe
D. The length of entrance region of pipe, in which full development of fluid flow takes place
E. h that velocity profile does not change downstream, is called the transition length
F. Transition length for turbulent flow of Newtonian fluids in a smooth pipe of diameter d is
A. Constant
C. All A., B. and C.
D. Affected by the fluid flow pressure
B. Surface tension
D. Inertial
A. 10 m
B. 30 m
D. 11.8 m
A. More than liquid vapor pressure
B. More than atmospheric pressure
C. Less than atmospheric pressure
A. Stream line body
B. None of these
C. Two dimensional body
A. V
B. V-0.8
C. V-1
A. Uniformly moving
B. Static
D. Accelerating frictionless
A. Sewage sludge
B. Rubber latex
D. Quicksand
A. Incompressible
B. Non-viscous
D. Neither A. nor B.
A. 1000
B. 3000
D. 2000
A. Run at a lower speed for the same discharge
B. Deliver fluid with pulsating/fluctuating discharge
D. Do not need priming
B. Fluid density
C. Surface tension
D. Gravity forces
B. Results in non-uniform discharge
C. Increases the work done
D. Causes cavitation
A. Altitude
B. Diameter
B. ? ?Q
C. ? Q2
D. ? Q
C. Water
D. Atmospheric air
A. Vane
B. Piston
D. Centrifugal
A. 0.66
B. 0.5
D. < 0.5
A. Archimedes principle
C. Newtons second law of motion
D. Newtons third law of motion
B. Pumping industrial wastes
C. Pumping liquid fertilisers (e.g. liquid NH3)
D. Booster service
A. f1 = f2
C. Data not sufficient to relate f1 & f2
D. f1 < f2
Showing 1 to 50 of 744 mcqs