4.1 s
5.2 s
10.4 s
14.1 s
C. 10.4 s
Venturimeter
Orifice plate
Nozzle
All of the above
Remains same
Decreases
Increases
None of these
w × Q × H
w × Q × hf
w × Q (H - hf)
w × Q (H + hf)
Less than 2000
Between 2000 and 4000
More than 4000
Less than 4000
Higher
Lower
Same
None of these
The flow is steady
The flow is streamline
Size and shape of the cross section in a particular length remain constant
Size and cross section change uniformly along length
Centre of gravity
Centre of pressure
Metacentre
Centre of buoyancy
Cohesion pressure is negligible
Cohesion pressure is decreased
Cohesion pressure is increased
There is no cohesion pressure
dQ/Q = (1/2) × (dH/H)
dQ/Q = (3/4) × (dH/H)
dQ/Q = (dH/H)
dQ/Q = (3/2) × (dH/H)
Inertia
Gravity
Viscous
None of these
Metacentre
Center of pressure
Center of buoyancy
Center of gravity
ML°T⁻²
ML°T
ML r²
ML²T²
Equal to
Double
Three to four times
Five to six times
Constant
Variable
Zero
Zero under limiting conditions
Bourdon tube
Pirani Gauge
Micro-manometer
Lonisation gauge
Metres² per sec
kg sec/metre
Newton-sec per metre
Newton-sec per metre
The size of orifice is large
The velocity of flow is large
The available head of liquid is more than 5 times the height of orifice
The available head of liquid is less than 5 times the height of orifice
4wd/σ cosα
σ cosα/4wd
4σ cosα/wd
wd/4σ cosα
It is the best liquid
The height of barometer will be less
Its vapour pressure is so low that it may be neglected
Both (B) and (C)
Pressure
Distance
Density
Flow
Rectangular
Triangular
Trapezoidal
Circular
Surface tension
Coefficient of viscosity
Viscosity
Osmosis
One dimensional flow
Uniform flow
Steady flow
Turbulent flow
tanθ = a/g
tanθ = 2 a/g
tanθ = a/2g
tanθ = a2/2g
Width of channel at the top is equal to twice the width at the bottom
Depth of channel is equal to the width at the bottom
The sloping side is equal to half the width at the top
The sloping side is equal to the width at the bottom
Absolute pressure
Velocity of fluid
Flow
Rotation
Mass of liquid displaced
Viscosity of the liquid
Pressure of the liquid displaced
Depth of immersion
Is steady and uniform
Takes place in straight line
Takes place in curve
Takes place in one direction
Directly proportional to the area of the vessel containing liquid
Directly proportional to the depth of liquid from the surface
Directly proportional to the length of the vessel containing liquid
Inversely proportional to the depth of liquid from the surface
Shear stress and the rate of angular distortion
Shear stress and viscosity
Shear stress, velocity and viscosity
Pressure, velocity and viscosity