Directly proportional to (radius)2
Inversely proportional to (radius)2
Directly proportional to (radius)4
Inversely proportional to (radius)4
C. Directly proportional to (radius)4
p/sinα
2p/sinα
p/2sinα
2p/sin (α/2)
N-m/s2
N-s/m2
Poise
Stoke
Low density
High density
Low surface tension
High surface tension
U-tube with water
Inclined U-tube
U-tube with mercury
Micro-manometer with water
Same as
Less than
More than
None of these
Steady flow
Turbulent flow
Vortex flow
Uniform flow
Length of both the pipes is same
Diameter of both the pipes is same
Loss of head and discharge of both the pipes is same
Loss of head and velocity of flow in both the pipes is same
Adhesion
Cohesion
Surface tension
Viscosity
Up-thrust
Buoyancy
Center of pressure
All the above are correct
ML°T⁻²
ML°T
ML r²
ML²T²
More
Less
Same
More or less depending on size of glass tube
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
Specific viscosity
Viscosity index
Kinematic viscosity
Coefficient of viscosity
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
Pascal law
Newton's law of viscosity
Boundary layer theory
Continuity equation
Notch
Weir
Mouthpiece
Nozzle
Capillary tube method
Orifice type viscometer
Rotating cylinder method
All of these
Q = (2/3) Cd × b × √(2g) × (H2 - H1)
Q = (2/3) Cd × b × √(2g) × (H2 1/2 - H1 1/2)
Q = (2/3) Cd × b × √(2g) × (H2 3/2 - H1 3/2)
Q = (2/3) Cd × b × √(2g) × (H2 2 - H1 2)
Centre of gravity
Centre of depth
Centre of pressure
Centre of immersed surface
A triangle
A paraboloid
An ellipse
None of these
Pressure in pipe, channels etc.
Atmospheric pressure
Very low pressures
Difference of pressure between two points
Elastic properties of the pipe material
Elastic properties of the liquid flowing through the pipe
Speed at which the valve is closed
All of the above
Directly proportional to the area of the vessel containing liquid
Directly proportional to the depth of liquid from the surface
Directly proportional to the length of the vessel containing liquid
Inversely proportional to the depth of liquid from the surface
1 Pa
91 Pa
981 Pa
9810 Pa
Circular
Square
Rectangular
Trapezoidal
Equal to
Directly proportional
Inversely proportional
None of these
Lift
Drag
Stagnation pressure
Bulk modulus
The fluid is non - viscous, homogeneous and incompressible
The velocity of flow is uniform over the section
The flow is continuous, steady and along the stream line
All of 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
Same as
Less than
More than
None of these