Pressure head
Velocity head
Pressure head + velocity head
Pressure head - velocity head
C. Pressure head + velocity head
wA
wx
wAx
wAx/sinθ
The area is horizontal
The area is vertical
The area is inclined
All of the above
Path line
Stream line
Steak line
Potential line
Centroid of the displaced volume of fluid
Center of pressure of displaced volume
Does not exist
None of the above
Open channel/pipe flow
Compressibility of fluids
Conservation of mass
Steady/unsteady flow
Same
Higher
Lower
Lower/higher depending on weight of body
The metacentre should lie above the center of gravity
The center of buoyancy and the center of gravity must lie on the same vertical line
A righting couple should be formed
All the above are correct
Steady uniform flow
Steady non-uniform flow
Unsteady uniform flow
Unsteady non-uniform flow
Linear
Parabolic
Hyperbolic
Inverse type
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 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
Cohesion
Adhesion
Viscosity
Surface tension
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
d = (D⁵/8fl)1/2
d = (D⁵/8fl)1/3
d = (D⁵/8fl)1/4
d = (D⁵/8fl)1/5
Specific gravity of liquids
Specific gravity of solids
Specific gravity of gases
Relative humidity
1 %
1.5 %
2 %
2.5 %
Is steady
Is one dimensional
Velocity is uniform at all the cross sections
All of the above
Has constant viscosity
Has zero viscosity
Is in compressible
None of the above
5 mm
10 mm
20 mm
30 mm
Weir
Notch
Orifice
None of these
Equal
Directly proportional
Inversely proportional
None of these
0.001
0.01
0.1
1
Equal to
Less than
More than
None of these
Increase in viscosity of gas
Increase in viscosity of liquid
Decrease in viscosity of gas
Decrease in viscosity of liquid
Incompressible
Compressible
Viscous
None of these
Shear stress and the rate of angular distortion
Shear stress and viscosity
Shear stress, velocity and viscosity
Pressure, velocity and viscosity
Length of both the pipes is same
Diameter of both the pipes is same
Loss of head and discharge of both the pipes is same
Loss of head and velocity of flow in both the pipes is same
Pressure
Flow
Shape
Volume
flv²/2gd
flv²/gd
3flv²/2gd
4flv²/2gd
Pressure
Flow
Velocity
Discharge