19.24 kPa
29.24 kPa
39.24 kPa
49.24 kPa
C. 39.24 kPa
Low pressure
Moderate pressure
High pressure
Atmospheric pressure
100 cm3
250 cm3
500 cm3
1000 cm3
Pressure, velocity and temperature
Shear stress and rate of shear strain
Shear stress and velocity
Rate of shear strain and temperature
Boyle's law
Archimedes principle
Pascal's law
Newton's formula
Kinematic viscosity in C. G. S. units
Kinematic viscosity in M. K. S. units
Dynamic viscosity in M. K. S. units
Dynamic viscosity in S. I. units
1
1.2
0.8
0.75
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
Fluids are capable of flowing
Fluids conform to the shape of the containing vessels
When in equilibrium, fluids cannot sustain tangential forces
When in equilibrium, fluids can sustain shear forces
A flow whose streamline is represented by a curve is called two dimensional flow.
The total energy of a liquid particle is the sum of potential energy, kinetic energy and pressure energy.
The length of divergent portion in a Venturimeter is equal to the convergent portion.
A pitot tube is used to measure the velocity of flow at the required point in a pipe.
Negligible
Same as buoyant force
Zero
None of the above
Bottom surface of the body
C.G. of the body
Metacentre
All points on the surface of the body
Incompressible
Compressible
Viscous
None of these
μπ²NR/60t
μπ²NR²/60t
μπ²NR³/60t
μπ²NR⁴/60t
4wd/σ cosα
σ cosα/4wd
4σ cosα/wd
wd/4σ cosα
Adhesion
Cohesion
Viscosity
Compressibility
Pressure energy + kinetic energy + potential energy
Pressure energy - (kinetic energy + potential energy)
Potential energy - (pressure energy + kinetic energy
Kinetic energy - (pressure energy + potential energy)
dQ/Q = (1/2) × (dH/H)
dQ/Q = (3/4) × (dH/H)
dQ/Q = (dH/H)
dQ/Q = (3/2) × (dH/H)
15.3 m
25.3 m
35.3 m
45.3 m
Pressure
Distance
Density
Flow
1.84 LH1/2
1.84 LH
1.84 LH3/2
1.84 LH5/2
Venturimeter
Orifice plate
Hot wire anemometer
Pitot tube
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
Total energy per unit discharge
Total energy measured with respect to the datum passing through the bottom of the channel
Total energy measured above the horizontal datum
Kinetic energy plotted above the free surface of water
Specific weight
Specific volume
Specific speed
Specific gravity
Pressure head
Velocity head
Pressure head + velocity head
Pressure head - velocity head
2gH
H × √(2g)
2g × √H
√(2gh)
Area of flow and wetted perimeter
Wetted perimeter and diameter of pipe
Velocity of flow and area of flow
None of these
Cd × a × √(2gH)
Cd × a × √(2g) × H3/2
Cd × a × √(2g) × H2
Cd × a × √(2g) × H5/2
One-dimensional flow
Two-dimensional flow
Three-dimensional flow
Four-dimensional flow
Notch
Weir
Mouthpiece
Nozzle