Pressure in pipes, channels etc.
Atmospheric pressure
Very low pressure
Difference of pressure between two points
B. Atmospheric pressure
Pressure force
Elastic force
Gravity force
Surface tension force
Steady flow
Unsteady flow
Laminar flow
Turbulent flow
Is uniform flow
Is steady uniform flow
Takes place in straight lines
Involves zero transverse component of flow
100 cm3
250 cm3
500 cm3
1000 cm3
At C.G. of body
At center of pressure
Vertically upwards
At metacentre
Total energy per unit discharge
Total energy measured with respect to the datum passing through the bottom of the channel
Total energy measured above the horizontal datum
Kinetic energy plotted above the free surface of water
Centre of gravity
Centre of pressure
Metacentre
Centre of buoyancy
dQ/Q = (1/2) × (dH/H)
dQ/Q = (3/4) × (dH/H)
dQ/Q = (dH/H)
dQ/Q = (3/2) × (dH/H)
Pascal's law
Dalton's law of partial pressure
Newton's law of viscosity
Avogadro's hypothesis
(bd²/12) + x
(d²/12 x) + x
b²/12 + x
d²/12 + x
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
Cohesion
Adhesion
Viscosity
Surface tension
Pressure in gases
Liquid discharge
Pressure in liquids
Gas velocities
Open channel/pipe flow
Compressibility of fluids
Conservation of mass
Steady/unsteady flow
Pressure head + kinetic head + potential head
Pressure head - (kinetic head + potential head)
Potential head - (pressure head + kinetic head)
Kinetic head - (pressure head + potential head)
1/RN
4/RN
16/RN
64/RN
25 kN/ m²
245 kN/ m²
2500 kN/m²
2.5 kN/ m²
C.G. of body
Center of pressure
Center of buoyancy
Metacentre
flv²/2gd
flv²/gd
3flv²/2gd
4flv²/2gd
One dimensional flow
Uniform flow
Steady flow
Turbulent flow
Orifice plate
Venturimeter
Rotameter
Pitot tube
Centroid of the volume of fluid vertically above the body
Centre of the volume of floating body
Center of gravity of any submerged body
Centroid of the displaced volume of fluid
15.3 m
25.3 m
35.3 m
45.3 m
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.
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)
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
Q = Cd × bH₁ × √(2gh)
Q = Cd × bH2 × √(2gh)
Q = Cd × b (H2 - H1) × √(2gh)
Q = Cd × bH × √(2gh)
Equal to
One-half
Three fourth
Double
2 metres of water column
3 metres of water column
3.5 metres of water column
4 m of water column
Moving
Viscous
Viscous and static
Viscous and moving