A. 0.1
B. 1
D. 0.94
A. Low capacity at low heads
C. High capacity at high heads
D. Low capacity at high heads
B. Variable
C. Both A. & B.
D. Neither A. nor B.
B. Discharge head
C. Suction lift
D. Specific gravity of the liquid
B. Inertial forces are unimportant and viscous forces control
C. Viscous forces predominate
D. None of these
A. One, which obeys Newtons law of viscosity
B. Highly viscous
C. None of these
A. Increases
B. None of these
D. Decreases
A. Fluid velocity decreases to zero
B. Total energy decreases
C. Both A. and B.
A. Globe
B. Gate
C. Needle
A. Submerged
B. Mono
D. Sump
A. Specific gravity
C. All A., B., and C.
D. Surface tension
A. Squeezes
B. Unpredictable from the data
C. Widens
B. Twice as that of A
C. Four times as that of A
D. Same as that of A
A. Pseudo-plastic
B. Dilatant
A. CD = 18.4/Re.p
B. 5.p
C. CD = 0.079/Re
D. CD = 16/Re.p
B. Bingham
D. Perfect
B. Remains unchanged
C. Decreases
D. Data insufficient to predict
A. Passing the centroid of the body at 60to the direction of motion
B. The component being normal to the flow direction
A. Fanning friction factor
B. Specific gravity
C. Euler number
A. 0
B. 0.5
C. ?
A. Either A. or B.
B. Greater than
D. Equal to
A. None of these
B. Loss of static head
D. Back flow through impeller
A. Diameter of
B. Fluid velocity leaving
C. Speed of
A. Regardless of the motion of one fluid layer relative to an adjacent layer
B. Only when the fluid is frictionless
D. Only when the fluid is at rest having zero velocity
B. For Reynolds number greater than 300
C. For unbaffled tank
B. Equipotential
D. Stream
B. Gear pump
C. Screw pump
D. Single stage centrifugal pump
A. > 1
C. < 2
D. 1
A. Used for mixing liquids of high viscosity
B. Radial flow mixers
C. Low speed impeller
A. 1/??
B. ?
D. ??
A. Radial
C. Mixed
B. 1.5
C. 1
D. 0.5
A. < 10
B. 4
A. Normal
C. Tangential
D. Convective
A. Compressibility is greater than zero
B. Temperature remains constant
C. Is frictionless
A. Rotameter
D. Manometer
A. Flow rate
C. Both a & b
D. Neither a nor b
A. Dilatant
C. Rheopectic
D. Thixotropic
A. Discharge pressure
B. Flow of liquid during operation of the pump
D. All A., B. and C.
B. Always the path of particle
C. A line connecting the mid points of flow cross-section
D. Drawn normal to the velocity vector at every point
A. Attained after moving one-half of total distance
B. A fluctuating velocity
A. 42
B. 1.8
D. 84
A. Speed
B. Impeller diameter
A. Bingham plastic
C. Dilatants
D. Newtonian
A. Deviating velocities
B. Pressure fluctuation
C. Eddies
A. ?Dp (?/1- ?)
B. ?Dp (1- ?/?)
D. (Dp/6) (1- ?/?)
A. Expanding tube at constant rate
C. Long pipe at decreasing rate
A. Pressure gradient
B. Absolute pressure
C. Gauge pressure
A. Thixotropic
D. Rheopectic
A. Water surface
C. Centre of buoyancy
Showing 6301 to 6350 of 8709 mcqs