Gas law
Boyle's law
Charles law
Pascal's law
B. Boyle's law
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
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
Steady uniform flow
Steady non-uniform flow
Unsteady uniform flow
Unsteady non-uniform flow
51 cm
50 cm
52 cm
52.2 cm
Has the dimensions of 1/pressure
Increases with pressure
Is large when fluid is more compressible
Is independent of pressure and viscosity
It is incompressible
It has uniform viscosity
It has zero viscosity
It is at rest
It has low vapour pressure
It is clearly visible
It has low surface tension
It can provide longer column due to low density
Resistance to shear stress is small
Fluid pressure is zero
Linear deformation is small
Only normal stresses can exist
At normal pressure of 760 mm
At 4°C temperature
At mean sea level
All the above
The pressure on the wall at the liquid level is minimum
The pressure on the bottom of the wall is maximum
The pressure on the wall at the liquid level is zero, and on the bottom of the wall is maximum
The pressure on the bottom of the wall is zer
0.46
0.64
0.78
0.87
15.3 m
25.3 m
35.3 m
45.3 m
1 and 2.5
2.5 and 4
4 and 6
1 and 6
Critical flow
Turbulent flow
Tranquil flow
Torrential flow
Only when the fluid is frictionless
Only when the fluid is incompressible and has zero viscosity
When there is no motion of one fluid layer relative to an adjacent layer
Irrespective of the motion of one fluid layer relative to an adjacent layer
Remain unaffected
Increases
Decreases
None of these
Lesser
Greater
Same
None of these
Does not change
Increases
Decreases
None of these
A × M × m1/2 × i2/3
A × M × m2/3 × i1/2
A1/2 × M2/3 × m × i
A2/3 × M1/3 × m × i
Z + p/w + v²/2g = constant
Z + p/w - v²/2g = constant
Z - p/w + v²/2g = constant
Z - p/w - v²/2g = constant
N-m/s
N-s/m2
m2/s
N-m
w
wh
w/h
h/w
Comparing two identical equipments
Designing models so that the result can be converted to prototypes
Comparing similarity between design and actual equipment
Hydraulic designs
Tensile stress
Compressive stress
Shear stress
Bending stress
Steady flow
Uniform flow
Streamline flow
Turbulent flow
Specific weight
Mass density
Specific gravity
None of these
Same as
Less than
More than
None of these
Friction loss and flow
Length and diameter
Flow and length
Friction factor and diameter
Double
Four times
Eight times
Sixteen times
Pressure force
Elastic force
Gravity force
Viscous force