Free
Partially
Full
None of these
C. Full
4wd/σ cosα
σ cosα/4wd
4σ cosα/wd
wd/4σ cosα
Less than
More than
Equal to
None of these
The metal piece will simply float over the mercury
The metal piece will be immersed in mercury by half
Whole of the metal piece will be immersed with its top surface just at mercury level
Metal piece will sink to the bottom
Atmospheric pressure
Pressure in pipes and channels
Pressure in Venturimeter
Difference of pressures between two points in a pipe
Gauge pressure + atmospheric pressure
Gauge pressure - atmospheric pressure
Atmospheric pressure - gauge pressure
Gauge pressure - vacuum pressure
The fluid is non - viscous, homogeneous and incompressible
The velocity of flow is uniform over the section
The flow is continuous, steady and along the stream line
All of the above
The nature of the liquid and the solid
The material which exists above the free surface of the liquid
Both of die above
Any one of the above
wH
wH/2
wH2/2
wH2/3
Specific gravity = gravity × density
Dynamic viscosity = kinematic viscosity × density
Gravity = specific gravity × density
Kinematic viscosity = dynamic viscosity × density
It gives maximum discharge for a given cross-sectional area and bed slope
It has minimum wetted perimeter
It involves lesser excavation for the designed amount of discharge
All of the above
1.84 LH1/2
1.84 LH
1.84 LH3/2
1.84 LH5/2
Surface tension
Compressibility
Capillarity
Viscosity
Sink to bottom
Float over fluid
Partly immersed
Be fully immersed with top surface at fluid surface
Shear stress and the rate of angular distortion
Shear stress and viscosity
Shear stress, velocity and viscosity
Pressure, velocity and viscosity
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
Reynold's number
Froude's number
Weber's number
Mach number
Mach number
Froude number
Reynoldss number
Weber's number
Vertical upward force through e.g. of body and center line of body
Buoyant force and the center line of body
Midpoint between e.g. and center of buoyancy
All of the above
0.83
0.6
0.4
0.3
0.417 H5/2
1.417 H5/2
4.171 H5/2
7.141 H5/2
Less than unity
Unity
Between 1 and 6
None of these
Equal to
Less than
More than
None of these
Remains constant
Increases
Decreases
Depends upon mass of liquid
Force of adhesion
Force of cohesion
Force of friction
Force of diffusion
Sum
Different
Product
Ratio
Same as
Lower than
Higher than
None of these
One dimensional flow
Uniform flow
Steady flow
Turbulent flow
Centre of gravity
Centre of pressure
Metacentre
Centre of buoyancy
Minimum
Maximum
Zero
Could be any value
Increases
Decreases
Remain unaffected
Unpredictable