A. Froude
C. Mach
D. Euler
B. 5
C. 1
D. 2
A. ersed</strong>
B. None of these
D. Is a variable head meter
E. Is an area meter
A. 0.5
B. 0.2
D. 0.8
A. None of these
B. Placed farther from the wall
D. Not affected by other particles and the wall
A. Blake-Plummer
C. Levas
D. Fanning friction factor
A. Schmidt number tends to infinity
B. Nusselt number tends to infinity
C. Archimedes number is greater than 10000
A. 64/NRe,P
B. 48/NRe,P
D. 16/NRe,P
A. Outer
D. Inner
B. Viscosity
C. Adhesion
D. Cohesion
B. 0.24
C. 24
D. 24000
B. 39.6y
C. 58y
D. 49.2y
A. Have lower operating costs
B. Have quieter operation
D. Require less space
A. Moderately viscous vegetable oil used in soap industry
C. None of the above
D. Molten sodium (used as a coolant in Fast Breeder Reactor)
B. As square of
C. Inversely as
D. Inversely as square root of
B. Pressure of liquids
C. Temperature of liquids
D. Velocity of liquids
A. P, Rand S
C. P and R
D. R and S
A. Decreases
C. Can either increase or decrease; depends on other factors
D. Remains unaltered
A. Pressure
B. Point velocity
D. Velocity head
A. Two
B. Three
D. Eight
A. Area through which fluid flows does not vary
C. None of these
D. Pressure drop increases linearly
B. Unsteady uniform flow
C. Steady uniform flow
D. Flow in a straight line
A. Vapour pressure of the liquid
C. Nature of the liquid being pumped
D. Power of the pump
A. Decreasing the diameter of the float
C. No means
D. Increasing the diameter of the float
B. Velocity head
D. Total pressure
B. 2v2/gc
C. ?.v2/2gc
D. ?v2/gc
A. Solids
C. Fluids
D. Liquids
B. Increases
C. Increases linearly
D. Decreases
A. 100 to 1000
B. 0.01 to 0.10
D. 200 to 300
A. 90bend
B. 45 elbow
D. T-joint
A. 7.65
C. 32.36
D. 48.22
A. Volute
B. Rotary vacuum
D. Centrifugal
A. Weber number
B. Euler number
D. Reynolds number
A. Flow of liquid upward in a vertical pipe
B. Impossible in a constant cross-section conduit
D. Flow of air downward in a pipe
A. That corresponding to static bed
C. Less than that of the static bed
D. That corresponding to completely fluidised bed
A. Trapezoidal
B. Rectangular
D. Triangular
A. Bingham plastic
B. Dilatent
C. Newtonian
B. Compressible fluids with shear
C. Compressible fluids with no shear
D. Incompressible fluids with shear
A. d2
C. d
D. d4
A. 4
B. 8
D. 5.5
A. Changing the speed of rotation
B. Bypassing liquid from the suction or discharge line
D. Bleeding air into suction
A. Elevation
C. Both A. & B.
D. Neither A. nor B.
A. The body should be bluff body
B. The main stream velocity must approach the velocity of sound in that fluid medium
C. The body should be stream lined
B. 3.7 KPa
C. 2.94 KPa
C. Reciprocating
D. Axial
A. 1/d
B. 1/?
A. Centroid of the volume of any floating body
B. Centre of gravity of a submerged body
A. Rotating vaned volute
C. Turbine type impeller
D. None of these
A. Reynolds number at the orifice
B. Ratio of orifice dia to pipe dia
D. None of the above parameters, and has a constant value of 0.61
A. Pseudo-plastic
B. Non-Newtonian
C. Dilatent
Showing 6351 to 6400 of 8709 mcqs