Maximum at the centre and minimum near the walls
Minimum at the centre and maximum near the walls
Zero at the centre and maximum near the walls
Maximum at the centre and zero near the walls
A. Maximum at the centre and minimum near the walls
4.1 s
5.2 s
10.4 s
14.1 s
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
The pressure at any location reaches an absolute pressure equal to the saturated vapour pressure of the liquid
Pressure becomes more than critical pressure
Flow is increased
Pressure is increased
Effects
Does not effect
Both A and B
None of these
Equal to
Less than
More than
None of these
Equal to
Less than
More than
None of these
Equal to
One-fourth
One-third
One-half
Less than twice
More than twice
Less than three times
More than three times
Atmospheric pressure
Gauge pressure
Absolute pressure
Mean pressure
Surface tension
Compressibility
Capillarity
Viscosity
0.0116 stoke
0.116 stoke
0.0611 stoke
0.611 stoke
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
2.4 m
3.0 m
4.0 m
5.0 m
Absolute pressure
Velocity of fluid
Flow
Rotation
Steady uniform flow
Steady non-uniform flow
Unsteady uniform flow
Unsteady non-uniform flow
Continuity equation
Bernoulli's equation
Pascal's law
Archimedess principle
More
Less
Same
More or less depending on size of glass tube
Moving
Viscous
Viscous and static
Viscous and moving
Notch
Weir
Mouthpiece
Nozzle
Z + p/w + v²/2g = constant
Z + p/w - v²/2g = constant
Z - p/w + v²/2g = constant
Z - p/w - v²/2g = constant
The weight of the body
More than the weight of the body
Less than the weight of the body
Weight of the fluid displaced by the body
2.89 kN
8.29 kN
9.28 kN
28.9 kN
The head loss for all the pipes is same
The total discharge is equal to the sum of discharges in the various pipes
The total head loss is the sum of head losses in the various pipes
Both (A) and (B)
Plus
Minus
Divide
Multiply
(2/3) × Cd (L - nH) × √(2gh)
(2/3) × Cd (L - 0.1nH) × √(2g) × H3/2
(2/3) × Cd (L - nH) × √(2g) × H²
(2/3) × Cd (L - nH) × √(2g) × H5/2
Equal to
Double
Three to four times
Five to six times
Running full
Running free
Partially running full
Partially running free
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
The center of gravity of the body and the metacentre
The center of gravity of the body and the center of buoyancy
The center of gravity of the body and the center of pressure
Center of buoyancy and metacentre
dp/ρ + g.dz + v.dv = 0
dp/ρ - g.dz + v.dv = 0
ρ.dp + g.dz + v.dv = 0
ρ.dp - g.dz + v.dv = 0