The nature of the liquid and the solid
The material which exists above the free surface of the liquid
Both of die above
Any one of the above
C. Both of die above
Avoid the tendency of breaking away the stream of liquid
To minimise frictional losses
Both (A) and (B)
None of these
Centre of gravity
Centre of pressure
Metacentre
Centre of buoyancy
Avoid interruption in the flow
Increase discharge
Increase velocity
Maintain pressure difference
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.
Comparing two identical equipments
Designing models so that the result can be converted to prototypes
Comparing similarity between design and actual equipment
Hydraulic designs
Up-thrust
Reaction
Buoyancy
Metacentre
Orifice plate
Venturimeter
Rotameter
Pitot tube
Increase
Remain unaffected
May increase or decrease depending on the characteristics of liquid
Decrease
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
Low pressure
High pressure
Low velocity
High velocity
Cannot be compressed
Occupy definite volume
Are not affected by change in pressure and temperature
None of the above
2.4 m above the hydraulic gradient
6.4 m above the hydraulic gradient
10.0 m above the hydraulic gradient
5.0 above the hydraulic gradient
Shear stress and the rate of angular distortion
Shear stress and viscosity
Shear stress, velocity and viscosity
Pressure, velocity and viscosity
Adhesion
Cohesion
Surface tension
Viscosity
Equal to
Double
Three to four times
Five to six times
Remains same
Decreases
Increases
None of these
Ratio of absolute viscosity to the density of the liquid
Ratio of density of the liquid to the absolute viscosity
Product of absolute viscosity and density of the liquid
Product of absolute viscosity and mass of the liquid
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
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
Constant
Variable
Zero
Zero under limiting conditions
Inertia force
Viscous force
Gravity force
Pressure force
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
At normal pressure of 760 mm
At 4°C temperature
At mean sea level
All the above
Sum
Difference
Arithmetic mean
Geometric mean
μ π³ N² R² /1800 t
μ π³ N² R⁴ /1800 t
μ π³ N² R² /3600 t
μ π³ N² R⁴ /3600 t
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
Sub-sonic flow
Sonic flow
Super-sonic flow
Hyper-sonic flow
Triangular
Rectangular
Square
Trapezoidal
Less than
More than
Equal to
None of these
p/sinα
2p/sinα
p/2sinα
2p/sin (α/2)