A. 1.5
B. 5
D. 0
B. Colebrook formula
C. None of these
D. Fanning equation
A. 42
B. 325
D. 26
A. Velocity of sound is reached
B. Valve is closed in a pipeline
D. Pressure reaches a minimum
A. Provided in the discharge line
B. Generally a globe valve
C. Provided to prevent liquid from backing up through the pump when the pump is turned off or
E. idently stops running
A. Submerged body
B. Volume of fluid vertically above the body
D. Horizontal projection of the body
A. ML-2T-2
B. ML-2T-1
A. Volumetric
B. Mechanical
C. Overall
B. 0.9
C. 0.03
D. 0.66
A. Inclined tube mercury
B. U-tube water
C. U-tube mercury
A. Pressure difference in pipe flow
B. Pressure at a point
C. Average flow velocity
A. d2/3
C. ?d
D. d1/3
A. High vibrations
C. Very low speeds
D. Smaller discharge
A. Same speed
B. Geometrical similarity
D. Same efficiency
A. Centrifugal
C. Diffuser
D. Plunger
A. None of these
B. Pitot tube
C. U-tube manometer
B. Opened
C. Either opened or closed; depending on the fluid viscosity
D. Either opened or closed; it does not make any difference
A. >25
B. 15 to 25
D. 2 to 5
B. Ideal/non i viscous fluids only
C. Irrotational flow only
A. (?H ?L) gL + (?L ?air)gH
C. (?H ?L)gH
D. (?H ?L) gH + (?L ?air) . g(L H)
A. D2
C. 1/D
D. 1/D2
A. ?p2
B. ?p/2
C. ?p
B. Skin
D. Disk
B. ?(?u)/?x = 0
C. ??/?t = 0
D. (?u/?x) = (??/?t)
A. Aid in rotational flow
B. None of these
C. Increase the structural strength of the tank
A. 100
B. 700
D. 2100
B. V1 < V2 < V3
D. V1 > V2 > V3
A. Newtonian
C. Viscous
D. Non-viscous
A. (V12 V22)/gc
B. (V12 V22)/2gc
D. (V1 V2)/2gc
A. Fluid velocity in the pipe
B. Time taken to close the valve
C. Pipe length
A. Water
C. Solids
B. 45 bend
C. 90 bend
D. 30 bend
A. 1
B. 10
C. 0.01
B. 160
C. 100
D. 320
A. Too high a suction lift
C. Low available NPSH and air leaks in the suction pipe
D. Incomplete priming
B. Low melting point semi-solids
C. Liquids
D. Powder & granular solids
A. Energy is constant along a streamline
B. Energy is not constant along a streamline
D. There exists a velocity potential
A. 1.25
C. 0.84
D. 0.5
A. Relates velocity and pressure
D. Is constant along an equipotential surface
B. Vs2/Dp3
C. Vs2/Dp2
D. Vs/Dp3
B. 550 kgf.m/second
C. Both A. and B.
D. 550 lbf.ft./hr
A. 80
C. 160
D. 120
B. At higher temperatures
D. Only in Newtonian fluids
A. Height of descend
B. Viscosity
D. Pressure
A. Non-viscous
B. Incompressible
B. Less than barometric pressure
C. Equal to the vapour pressure of the liquid
D. Less than the vapour pressure of the liquid
A. Efficiency, B.H.P. and head
B. Efficiency, head and B.H.P.
D. B.H.P., efficiency and head
A. Parabolic
B. Flat
D. Flat near the wall and parabolic in the middle
B. Achieve the exact delivery pressure
D. Cool the delivered air
B. Specific weight
D. Volume
Showing 6651 to 6700 of 8709 mcqs