100 litres
250 litres
500 litres
1000 litres
D. 1000 litres
Fluid
Water
Gas
Ideal fluid
Has constant viscosity
Has zero viscosity
Is in compressible
None of the above
14π R1/2/15Cd × a √(2g)
14π R3/2/15Cd × a √(2g)
14π R5/2/15Cd × a √(2g)
14π R7/2/15Cd × a √(2g)
Pascal's law
Archimedess principle
Principle of floatation
Bernoulli's theorem
0.34 times
0.67 times
0.81 times
0.95 times
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
Atmospheric pressure
Pressure in pipes and channels
Pressure in Venturimeter
Difference of pressures between two points in a pipe
Less man the vapour pressure over the plane surface
Equal to the vapour pressure over the plane surface
Greater than the vapour pressure over the plane surface
Zero
Pressure head
Velocity head
Pressure head + velocity head
Pressure head - velocity head
0.3 to 0.45
0.50 to 0.75
0.75 to 0.95
0.95 to 1.0
Dissolved air
Dissolved salt
Suspended matter
All of the above
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
Velocity of liquid
Pressure of liquid
Area of mouthpiece
Length of mouthpiece
50 %
56.7 %
66.67 %
76.66 %
2A × √H₁/Cd × a × √(2g)
2A × √H₂/Cd × a × √(2g)
2A × (√H₁ - √H₂)/Cd × a × √(2g)
2A × (√H3/2 - √H3/2)/Cd × a × √(2g)
A × √(m × i)
C × √(m × i)
AC × √(m × i)
mi × √(A × C)
Density of liquid
Specific gravity of liquid
Compressibility of liquid
Surface tension of liquid
0.62
0.76
0.84
0.97
1.84 LH1/2
1.84 LH
1.84 LH3/2
1.84 LH5/2
One dimensional flow
Streamline flow
Steady flow
Turbulent flow
Mass
Momentum
Energy
Work
The resultant force acting on a floating body
The resultant force on a body due to the fluid surrounding it
Equal to the volume of liquid displaced
The force necessary to maintain equilibrium of a submerged body
Centroid of the displaced volume of fluid
Center of pressure of displaced volume
Does not exist
None of the above
Narrow crested weir
Broad crested weir
Ogee weir
Submerged weir
Increase
Remain unaffected
May increase or decrease depending on the characteristics of liquid
Decrease
Path line
Stream line
Steak line
Potential line
Absolute temperature
Temperature
Density
Modulus of elasticity
0.384 Cd × L × H1/2
0.384 Cd × L × H3/2
1.71 Cd × L × H1/2
1.71 Cd × L × H3/2
0.375
0.5
0.707
0.855
Constant
Variable
Zero
Zero under limiting conditions