Less than 2000
Between 2000 and 2800
More than 2800
None of these
C. More than 2800
There is no loss of energy of the liquid flowing
The velocity of flow is uniform across any cross-section of the pipe
No force except gravity acts on the fluid
All of the above
Equal to
One-fourth
One-third
One-half
Straight line
Parabolic curve
Hyperbolic curve
Elliptical
Ratio of inertial force to force due to viscosity
Ratio of inertial force to force due to gravitation
Ratio of inertial force to force due to surface tension
All the four ratios of inertial force to force due to viscosity, gravitation, surface tension, and elasticity
At C.G. of body
At center of pressure
Vertically upwards
At metacentre
It has low vapour pressure
It is clearly visible
It has low surface tension
It can provide longer column due to low density
Same as
Lower than
Higher than
None of these
1 %
1.5 %
2 %
2.5 %
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.
There is excessive leakage in the pipe
The pipe bursts under high pressure of fluid
The flow of fluid through the pipe is suddenly brought to rest by closing of the valve
The flow of fluid through the pipe is gradually brought to rest by closing of the valve
At the centre of gravity
Above the centre of gravity
Below be centre of gravity
Could be above or below e.g. depending on density of body and liquid
Decreases
Increases
Remain same
None of these
(2A√H₁)/(Cd × a√2g)
(2AH₁)/(Cd × a√2g)
(2AH₁3/2)/(Cd × a√2g)
(2AH₁²)/(Cd × a√2g)
Friction loss and flow
Length and diameter
Flow and length
Friction factor and diameter
Directly proportional to density of fluid
Inversely proportional to density of fluid
Directly proportional to (density)1/2 of fluid
Inversely proportional to (density)1/2 of fluid
π w ω² r²/4g
π w ω² r³/4g
π w ω² r⁴/4g
π w ω² r²/2g
Venturimeter
Orifice plate
Hot wire anemometer
Pitot tube
Tension at the base
Overturning of the wall or dam
Sliding of the wall or dam
All of these
Remains constant
Increases
Decreases
Depends upon mass of liquid
Double
Four times
Eight times
Sixteen times
400 kg/cm²
4000 kg/cm²
40 × 10⁵ kg/cm²
40 × 10⁶ kg/cm²
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
0.384 Cd × L × H1/2
0.384 Cd × L × H3/2
1.71 Cd × L × H1/2
1.71 Cd × L × H3/2
Pascal's law
Dalton's law of partial pressure
Newton's law of viscosity
Avogadro's hypothesis
0.5 a. √2gH
0.707 a. √2gH
0.855 a. √2gH
a. √2gH
2gH
H × √(2g)
2g × √H
√(2gh)
Concave
Convex
Plane
None of these
The pressure below the nappe is atmospheric
The pressure below the nappe is negative
The pressure above the nappe is atmospheric
The pressure above the nappe is negative
N-m/s
N-s/m2
m2/s
N-m
Area of flow and wetted perimeter
Wetted perimeter and diameter of pipe
Velocity of flow and area of flow
None of these