1 and 2.5
2.5 and 4
4 and 6
1 and 6
D. 1 and 6
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
Weir
Notch
Orifice
None of these
ML°T⁻²
ML°T
ML r²
ML²T²
Circular
Square
Rectangular
Trapezoidal
N/m
N/m2
N/m3
N-m
dQ/Q = 3/2 × (dH/H)
dQ/Q = 2 × (dH/H)
dQ/Q = 5/2 × (dH/H)
dQ/Q = 3 × (dH/H)
π w ω² r²/4g
π w ω² r³/4g
π w ω² r⁴/4g
π w ω² r²/2g
Centroid of the volume of fluid vertically above the body
Centre of the volume of floating body
Center of gravity of any submerged body
Centroid of the displaced volume of fluid
Pressure
Velocity
Square of velocity
Cube of velocity
1 and 2.5
2.5 and 4
4 and 6
1 and 6
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
Pressure
Distance
Density
Flow
1
1000
100
101.9
Pressure force
Elastic force
Gravity force
Surface tension force
Shear stress and the rate of angular distortion
Shear stress and viscosity
Shear stress, velocity and viscosity
Pressure, velocity and viscosity
Has constant viscosity
Has zero viscosity
Is in compressible
None of the above
h
wh
w/h
h/w
C.G. of body
Center of pressure
Center of buoyancy
Metacentre
Bottom surface of the body
C.G. of the body
Metacentre
All points on the surface of the body
Equal to
Less than
More than
None of these
Remain same
Increases
Decreases
Shows erratic behaviour
N-m/s
N-s/m2
m2/s
N-m
1000 N/m3
10000 N/m3
9.81 × 103 N/m3
9.81 × 10⁶ N/m3
Quasi-static
Steady state
Laminar
Uniform
Steady flow
Turbulent flow
Laminar flow
Non-uniform flow
ρ ω2 r2
2ρ ω2 r2
ρ ω2 r2/2
ρ ω2 r2/4
Actual velocity of jet at vena-contracta to the theoretical velocity
Area of jet at vena-contracta to the area of orifice
Loss of head in the orifice to the head of water available at the exit of the orifice
Actual discharge through an orifice to the theoretical discharge
Volumetric strain
Volumetric index
Compressibility
Adhesion
w1a1 = w2a2
w1v1 = w2v2
a1v1 = a2v2
a1/v1 = a2/v2
Velocity of liquid
Atmospheric pressure
Pressure in pipes and channels
Difference of pressure between two points in a pipe