(2/3) Cd × L.√2g [H1 - Ha]
(2/3) Cd × L. √2g [H1 3/2 - Ha 3/2]
(2/3) Cd × L.√2g [H1 2 - Ha 2]
(2/3) Cd × L. √2g [H1 5/2 - Ha 5/2]
B. (2/3) Cd × L. √2g [H1 3/2 - Ha 3/2]
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
Mass of liquid displaced
Viscosity of the liquid
Pressure of the liquid displaced
Depth of immersion
Shear stress to shear strain
Increase in volume to the viscosity of fluid
Increase in pressure to the volumetric strain
Critical velocity to the viscosity of fluid
Remains horizontal
Becomes curved
Falls on the front end
Falls on the back end
(μπ²N/60t) × (R₁ - R₂)
(μπ²N/60t) × (R₁² - R₂²)
(μπ²N/60t) × (R₁³ - R₂³)
(μπ²N/60t) × (R₁⁴ - R₂⁴)
Cannot be compressed
Occupy definite volume
Are not affected by change in pressure and temperature
None of the above
Higher than the surface of liquid
The same as the surface of liquid
Lower than the surface of liquid
Unpredictable
Directly proportional to its distance from the centre
Inversely proportional to its distance from the centre
Directly proportional to its (distance)2 from the centre
Inversely proportional to its (distance)2 from the centre
Higher
Lower
Same
Higher/lower depending on temperature
ML°T⁻²
ML°T
ML r²
ML²T²
Directly proportional
Inversely proportional
Square root of velocity
None of these
d/6
d/4
d/2
d
Inversely proportional to H3/2
Directly proportional to H3/2
Inversely proportional to H5/2
Directly proportional to H5/2
Newton's law of motion
Newton's law of viscosity
Pascal' law
Continuity equation
Negligible
Same as buoyant force
Zero
None of the above
Steady flow
Unsteady flow
Laminar flow
Uniform flow
Steady uniform
Non-steady non-uniform
Non-steady uniform
Steady non-uniform
Pressure, velocity and temperature
Shear stress and rate of shear strain
Shear stress and velocity
Rate of shear strain and temperature
Pressure energy + kinetic energy + potential energy
Pressure energy - (kinetic energy + potential energy)
Potential energy - (pressure energy + kinetic energy
Kinetic energy - (pressure energy + potential energy)
Equal to
Directly proportional
Inversely proportional
None of these
Decreases
Increases
Remain same
None of these
v²/2g
0.5v²/2g
0.375v²/2g
0.75v²/2g
Specific weight
Specific mass
Specific gravity
Specific density
Pressure force
Elastic force
Gravity force
Viscous force
Are viscous
Possess surface tension
Are compressible
Possess all the above properties
Atmospheric pressure
Surface tension
Force of adhesion
Force of cohesion
Wake
Drag
Lift
Boundary layer
Centre of gravity
Centre of depth
Centre of pressure
Centre of immersed surface
Higher
Lower
Same
None of these
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.