Equal to
One-fourth
One-third
One-half
B. One-fourth
More
Less
Same
More or less depending on size of glass tube
ρ ω2 r2
2ρ ω2 r2
ρ ω2 r2/2
ρ ω2 r2/4
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)
Tensile stress
Compressive stress
Shear stress
Bending stress
Pressure
Flow
Velocity
Discharge
Pressure
Flow
Shape
Volume
Sub-sonic flow
Sonic flow
Super-sonic flow
Hyper-sonic flow
Directly
Inversely
Both A and B
None of these
Vertical upward force through e.g. of body and center line of body
Buoyant force and the center line of body
Midpoint between e.g. and center of buoyancy
All of the above
Atmospheric pressure
Pressure in pipes and channels
Pressure in Venturimeter
Difference of pressures between two points in a pipe
Pressure force
Elastic force
Surface tension force
Viscous force
Atmospheric pressure
Gauge pressure
Absolute pressure
None of these
Constant
Variable
Zero
Zero under limiting conditions
One stoke
One centistoke
One poise
One centipoise
Any weight, floating or immersed in a liquid, is acted upon by a buoyant force
Buoyant force is equal to the weight of the liquid displaced
The point through which buoyant force acts, is called the center of buoyancy
Center of buoyancy is located above the center of gravity of the displaced liquid
Pressure in pipes, channels etc.
Atmospheric pressure
Very low pressure
Difference of pressure between two points
Steady uniform
Non-steady non-uniform
Non-steady uniform
Steady non-uniform
500 kg
1000 kg
1500 kg
2000 kg
Sub-sonic velocity
Super-sonic velocity
Lower critical velocity
Higher critical velocity
Adhesion
Cohesion
Viscosity
Compressibility
Planes of the body are completely smooth
Space around the body is completely filled with the fluid
Fluid particles do not exert any influence on one another
All of the above
(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]
Venturimeter
Orifice plate
Nozzle
All of the above
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
Water surface
Center of pressure
Center of gravity
Center of buoyancy
The liquid particles at all sections have the same velocities
The liquid particles at different sections have different velocities
The quantity of liquid flowing per second is constant
Each liquid particle has a definite path
Gravitational force is equal to the up-thrust of the liquid
Gravitational force is less than the up-thrust of the liquid
Gravitational force is more than the up-thrust of the liquid
None of the above
Vacuum pressure
Gauge pressure
Absolute pressure
Atmospheric pressure
Cannot be subjected to shear forces
Always expands until it fills any container
Has the same shear stress at a point regardless of its motion
Cannot remain at rest under action of any shear force
Velocity of flow in an open channel
Depth of flow in an open channel
Hydraulic jump
Depth of channel