Increases
Decreases
Remain constant
Increases first up to certain limit and then decreases
A. Increases
Mach number
Froude number
Reynolds number
Weber's number
Actual velocity of jet at vena contracta to the theoretical velocity
Area of jet at vena contracta to the area of orifice
Actual discharge through an orifice to the theoretical discharge
None of the above
Frictional force
Viscosity
Surface friction
All of the above
Actual velocity of jet at vena contracta to the theoretical velocity
Loss of head in the orifice to the head of water available at the exit of the orifice
Loss of head in the orifice to the head of water available at the exit of the orifice
Area of jet at vena-contracta to the area of orifice
Resistance to shear stress is small
Fluid pressure is zero
Linear deformation is small
Only normal stresses can exist
Resultant force acting on a floating body
Equal to the volume of liquid displaced
Force necessary to keep a body in equilibrium
The resultant force on a body due to the fluid surrounding it
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
Increase in viscosity of gas
Increase in viscosity of liquid
Decrease in viscosity of gas
Decrease in viscosity of liquid
0.417 H5/2
1.417 H5/2
4.171 H5/2
7.141 H5/2
Narrow crested weir
Broad crested weir
Ogee weir
Submerged weir
Q = Cd × bH₁ × √(2gh)
Q = Cd × bH2 × √(2gh)
Q = Cd × b (H2 - H1) × √(2gh)
Q = Cd × bH × √(2gh)
One-fourth of the total supply head
One-third of the total supply head
One-half of the total supply head
Two-third of the total supply head
Centre of gravity
Centre of depth
Centre of pressure
Centre of immersed surface
ω.r/2g
ω².r²/2g
ω.r/4g
ω².r²/4g
One dimensional flow
Streamline flow
Steady flow
Turbulent flow
3.53 kN
33.3 kN
35.3 kN
None of these
Same as
Less than
More than
None of these
Is steady
Is one dimensional
Velocity is uniform at all the cross sections
All of the above
Remains constant
Increases
Decreases
Depends upon mass of liquid
Neutral equilibrium
Stable equilibrium
Unstable equilibrium
None of these
An equivalent pipe is treated as an ordinary pipe for all calculations
The length of an equivalent pipe is equal to that of a compound pipe
The discharge through an equivalent pipe is equal to that of a compound pipe
The diameter of an equivalent pipe is equal to that of a compound pipe
Surface tension
Capillarity
Viscosity
Shear stress in fluids
0.62
0.76
0.84
0.97
Same as
Less than
More than
None of these
The direction and magnitude of the velocity at all points are identical
The velocity of successive fluid particles, at any point, is the same at successive periods of time
The magnitude and direction of the velocity do not change from point to point in the fluid
The fluid particles move in plane or parallel planes and the streamline patterns are identical in each plane
There is no loss of energy of the liquid flowing
The velocity of flow is uniform across any cross-section of the pipe
No force except gravity acts on the fluid
All of the above
At normal pressure of 760 mm
At 4°C temperature
At mean sea level
All the above
2gH
H × √(2g)
2g × √H
√(2gh)
Cannot be subjected to shear forces
Always expands until it fills any container
Has the same shear stress at a point regardless of its motion
Cannot remain at rest under action of any shear force
Low pressure
High pressure
Moderate pressure
Vacuum pressure