Option A: Change in direction of flow
Option B: Change in total energy
Option C: Change in pressure
Option D: Non uniform direction of velocities at inlet & outlet sections
Correct Answer: Non uniform direction of velocities at inlet & outlet sections ✔
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Option A: Sump
Option B: Volute
Option C: Vacuum
Option D: Submerged
Correct Answer: Vacuum ✔
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Option A: Employs such an impeller, through which the flow is a combination of radial & axial flow
Option B: Mixes the two fluids before pumping them
Option C: Pumps the two fluids separately and then mixes them
Option D: Employs impellers in both the radial & axial directions
Correct Answer: Employs such an impeller, through which the flow is a combination of radial & axial flow ✔
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Option A: Blower
Option B: Compressor
Option C: Vacuum pump
Option D: Fan
Correct Answer: Vacuum pump ✔
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Option A: G is above B
Option B: B is above G
Option C: B & G coincide
Option D: None of these
Correct Answer: B is above G ✔
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Option A: Kinetic head gets converted into static head
Option B: Moving stream gradually reduces velocity
Option C: Mean velocity remains constant
Option D: None of these
Correct Answer: Kinetic head gets converted into static head ✔
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Option A: More
Option B: Less
Option C: Same
Option D: Unpredictable
Correct Answer: More ✔
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Option A: 1,300
Option B: 10,000
Option C: 100,000
Option D: None of these
Correct Answer: 1,300 ✔
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Option A: Use of floats of different densities
Option B: No means
Option C: Increasing the diameter of the float
Option D: Decreasing the diameter of the float
Correct Answer: Use of floats of different densities ✔
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Option A: Axial flow mixers
Option B: Low speed impeller
Option C: Used for mixing liquids of high viscosity
Option D: Radial flow mixers
Correct Answer: Axial flow mixers ✔
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Option A: Less than the vapour pressure of the liquid at that temperature
Option B: Greater than the vapour pressure of the liquid at that temperature
Option C: Equal to the vapour pressure
Option D: Equal to the developed head
Correct Answer: Less than the vapour pressure of the liquid at that temperature ✔
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Option A: Cavitation
Option B: Low speed of impeller
Option C: Its operation with delivery valve closed for considerable time after starting the pump
Option D: Off centering of pump with motor
Correct Answer: Cavitation ✔
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Option A: Is always below
Option B: Is the evolute of
Option C: Intersects at right angle
Option D: Is tangential to
Correct Answer: Is the evolute of ✔
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Option A: Narrow
Option B: Deep
Option C: Both A. & B.
Option D: Neither A. nor B.
Correct Answer: C. Both A. & B. ✔
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Option A: Long pipe at constant rate
Option B: Long pipe at decreasing rate
Option C: Expanding tube at increasing rate
Option D: Expanding tube at constant rate
Correct Answer: Expanding tube at increasing rate ✔
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Option A: Vavg
Option B: 1.2 Vavg
Option C: 1.5 Vavg
Option D: 1.8 Vavg
Correct Answer: Vavg ✔
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Option A: Parabolic law
Option B: Linear law
Option C: Logarithmic law
Option D: None of these
Correct Answer: Logarithmic law ✔
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Option A: Turbulent flow
Option B: Laminar flow through an open channel
Option C: Steady flow
Option D: None of these
Correct Answer: None of these ✔
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Option A: Fluid flow at the inlet to a nozzle
Option B: Fluid flow between parallel plates
Option C: Viscous fluid flow between converging plates
Option D: None of these
Correct Answer: Fluid flow at the inlet to a nozzle ✔
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Option A: Elevation & kinetic energy
Option B: Elevation & pressure
Option C: Kinetic energy & pressure
Option D: None of these
Correct Answer: Elevation & pressure ✔
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Option A: Press
Option B: Turbine
Option C: Pump
Option D: Coupling
Correct Answer: Press ✔
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Option A: Reduce the cost of compressor
Option B: Reduce the size requirement
Option C: Resemble closely to isothermal compression
Option D: Are easy to control
Correct Answer: Resemble closely to isothermal compression ✔
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Option A: MLT-1
Option B: L2T-1
Option C: L2T
Option D: L2T-2
Correct Answer: L2T-1 ✔
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In case of Couette flow, the fluid flow is between two large flat parallel plates with__________?
Option A: Top plate moving and the bottom plate fixed
Option B: Bottom plate moving and the top plate fixed
Option C: Both the plates fixed
Option D: Both the plates moving
Correct Answer: Top plate moving and the bottom plate fixed ✔
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Option A: Surface tension
Option B: Gravity
Option C: Viscous
Option D: Elastic
Correct Answer: Surface tension ✔
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Option A: Compressible fluids with shear
Option B: Compressible fluids with no shear
Option C: Incompressible fluids with shear
Option D: Incompressible fluids with no shear
Correct Answer: Incompressible fluids with no shear ✔
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Option A: Heat conduction to viscosity of a fluid
Option B: Cp/Cv of a fluid
Option C: Elastic force to pressure force in the fluid flow
Option D: Inertial force to elastic force in the fluid flow
Correct Answer: Heat conduction to viscosity of a fluid ✔
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Option A: Non-steady uniform
Option B: Non-steady non-uniform
Option C: Steady uniform
Option D: Steady non-uniform
Correct Answer: Non-steady uniform ✔
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Option A: (Dp/6) (ε/1- ε)
Option B: (Dp/6) (1- ε/ε)
Option C: ⅔Dp (1- ε/ε)
Option D: ⅔Dp (ε/1- ε)
Correct Answer: (Dp/6) (ε/1- ε) ✔
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Option A: Only when the fluid is frictionless
Option B: Only when the fluid is at rest having zero velocity
Option C: When there is no motion of one fluid layer relative to an adjacent layer
Option D: Regardless of the motion of one fluid layer relative to an adjacent layer
Correct Answer: When there is no motion of one fluid layer relative to an adjacent layer ✔
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Option A: Velocity of liquids
Option B: Temperature of liquids
Option C: Velocity of gases
Option D: Pressure of liquids
Correct Answer: Velocity of gases ✔
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Option A: 1.8
Option B: 12.4
Option C: 186.2
Option D: 736.4
Correct Answer: 12.4 ✔
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Option A: Newtonian
Option B: Pseudo-plastic
Option C: Dilatent
Option D: Bingham plastic
Correct Answer: Pseudo-plastic ✔
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Option A: Bingham plastic
Option B: Dilatant
Option C: Newtonian
Option D: Pseudo plastic
Correct Answer: Dilatant ✔
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Option A: Back flow through impeller
Option B: Loss of kinetic head
Option C: Loss of static head
Option D: None of these
Correct Answer: Loss of kinetic head ✔
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Option A: CD = 16/Re.p
Option B: CD = 24/Re.p
Option C: CD = 18.4/Re.p
Option D: CD = 0.079/Re
Correct Answer: CD = 24/Re.p ✔
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Option A: Q = Q1 + Q2 + Q3
Option B: V1 = V2 = V3
Option C: Q1 = Q2 = Q3
Option D: f = f1 + f2 + f3
Correct Answer: Q = Q1 + Q2 + Q3 ✔
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Option A: Needle
Option B: Globe
Option C: Gate
Option D: Butterfly
Correct Answer: Needle ✔
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Option A: Changing the speed of rotation
Option B: Bleeding air into suction
Option C: Bypassing liquid from the suction or discharge line
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Generally a needle valve
Option B: Used to release any gases that might be vapour locking the pump
Option C: Helpful in easy removal of samples
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Dilatant
Option B: Bingham plastic
Option C: Newtonian
Option D: Pseudo-plastic
Correct Answer: Bingham plastic ✔
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Option A: Passing the centroid of the body at 60°to the direction of motion
Option B: The component being parallel to the flow direction
Option C: The component being normal to the flow direction
Option D: None of these
Correct Answer: The component being parallel to the flow direction ✔
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Option A: It is not very accurate
Option B: It is very costly
Option C: Most of the pressure drop is not recoverable
Option D: It is not suitable for measuring gas flow
Correct Answer: Most of the pressure drop is not recoverable ✔
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Option A: Of real fluids
Option B: Over flat surfaces only
Option C: In pipes only
Option D: Of ideal fluids only
Correct Answer: Of real fluids ✔
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Option A: Pressure fluctuation
Option B: Eddies
Option C: Deviating velocities
Option D: All A., B. & C.
Correct Answer: D. All A., B. & C. ✔
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Option A: Dependent on the speed of the pump
Option B: Dependent on the power of the pump
Option C: 34 feet
Option D: 150 feet
Correct Answer: 34 feet ✔
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Option A: Directly as
Option B: Inversely as square root of
Option C: Inversely as
Option D: As square of
Correct Answer: Directly as ✔
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Option A: Develops a lower head
Option B: Capacity is reduced
Option C: Requires more power
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Δp
Option B: < Δp
Option C: > Δp
Option D: Δp2
Correct Answer: Δp ✔
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Option A: Reynolds number at the orifice
Option B: Ratio of orifice dia to pipe dia
Option C: Both A. and B.
Option D: None of the above parameters, and has a constant value of 0.61
Correct Answer: C. Both A. and B. ✔
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Option A: That is traced by all the fluid particles passing through a given point
Option B: Along which a fluid particle travels
Option C: Such that at every point on it, the velocity is tangential to it
Option D: None of these
Correct Answer: Such that at every point on it, the velocity is tangential to it ✔
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Option A: Total pressure
Option B: Total energy
Option C: Velocity head
Option D: None of these
Correct Answer: Total energy ✔
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Option A: Fluid particles move in an orderly manner
Option B: Momentum transfer is on molecular scale only
Option C: Shear stress is caused more effectively by cohesion than momentum transfer
Option D: Shear stresses are generally larger than in a similar laminar flow
Correct Answer: Shear stresses are generally larger than in a similar laminar flow ✔
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Option A: Very precise control of
Option B: Unidirectional
Option C: Multidirectional
Option D: None of these
Correct Answer: Unidirectional ✔
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Option A: For Reynolds number greater than 300
Option B: When there is no vortex formation
Option C: For unbaffled tank
Option D: None of these
Correct Answer: When there is no vortex formation ✔
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Option A: Reciprocating
Option B: Centrifugal
Option C: Volute
Option D: Rotary vacuum
Correct Answer: Reciprocating ✔
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Option A: H1/2
Option B: H5/2
Option C: H2/5
Option D: H3/2
Correct Answer: H3/2 ✔
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Option A: Velocity head
Option B: Pressure
Option C: Point velocity
Option D: None of these
Correct Answer: None of these ✔
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Option A: Temperature remains constant
Option B: Compressibility is greater than zero
Option C: Density does not change with pressure & temperature
Option D: Is frictionless
Correct Answer: Density does not change with pressure & temperature ✔
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Option A: Sewage sludge
Option B: Rubber latex
Option C: Blood
Option D: Sugar solution
Correct Answer: Sewage sludge ✔
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Option A: Flow of liquid upward in a vertical pipe
Option B: Flow through a converging section
Option C: Flow of air downward in a pipe
Option D: Impossible in a constant cross-section conduit
Correct Answer: Flow through a converging section ✔
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Option A: Fluid flow rate & friction loss
Option B: Length & friction factor
Option C: Diameter & friction factor
Option D: Length & diameter
Correct Answer: Fluid flow rate & friction loss ✔
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Option A: Euler
Option B: Froude
Option C: Mach
Option D: Weber
Correct Answer: Weber ✔
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Option A: Corresponding to uniform flow
Option B: Measured normal to the channel bed
Option C: Corresponding to steady flow
Option D: None of these
Correct Answer: Corresponding to uniform flow ✔
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Option A: Potential
Option B: Streamline
Option C: Creep
Option D: Boundary layer
Correct Answer: Potential ✔
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Option A: Molten sodium (used as a coolant in Fast Breeder Reactor)
Option B: Moderately viscous vegetable oil used in soap industry
Option C: Thick molten soap at 80°C
Option D: None of the above
Correct Answer: Thick molten soap at 80°C ✔
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Option A: Circular
Option B: Rectangular
Option C: Triangular
Option D: Trapezoidal
Correct Answer: Circular ✔
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Option A: Frictionless & incompressible
Option B: One, which obeys Newton’s law of viscosity
Option C: Highly viscous
Option D: None of these
Correct Answer: Frictionless & incompressible ✔
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Option A: Paddle
Option B: Turbine
Option C: Propeller
Option D: All A., B. and C.
Correct Answer: Propeller ✔
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Option A: Water surface
Option B: Centre of gravity
Option C: Centre of buoyancy
Option D: None of these
Correct Answer: Centre of gravity ✔
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Option A: Rheopectic
Option B: Pseudo-plastic
Option C: Thixotropic
Option D: Dilatant
Correct Answer: Pseudo-plastic ✔
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Option A: 4
Option B: 2100-4000
Option C: 4000
Option D: ∞
Correct Answer: ∞ ✔
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Option A: V/Vmax = (x/r)1/7
Option B: V/Vmax = (r/x)1/7
Option C: V/Vmax = (x.r)1/7
Option D: None of these
Correct Answer: V/Vmax = (x/r)1/7 ✔
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Option A: Longer, if Metacentric height is increased
Option B: Independent of the Metacentric height
Option C: Dependent on the buoyant forces only
Option D: None of these
Correct Answer: None of these ✔
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Option A: Newtonian
Option B: Dilatant
Option C: Pseudo-plastic
Option D: Non-Newtonian
Correct Answer: Newtonian ✔
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Option A: Is an area meter
Option B: Is a variable head meter
Option C: Rotates an element at a speed determined by the velocity of the fluid in which the meter is
Option D: None of these
Correct Answer: C. Rotates an element at a speed determined by the velocity of the fluid in which the meter is
immersed ✔
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Option A: Corrosive
Option B: Viscous
Option C: Non-Newtonian
Option D: Solid suspended
Correct Answer: Corrosive ✔
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Option A: The body should be bluff body
Option B: The body should be stream lined
Option C: Circulation around the body is essentially required
Option D: The main stream velocity must approach the velocity of sound in that fluid medium
Correct Answer: Circulation around the body is essentially required ✔
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Option A: Reduction of pressure below vapour pressure
Option B: Reduction of pressure gradient to zero
Option C: Adverse pressure gradient
Option D: Reduction of boundary layer thickness to zero
Correct Answer: Adverse pressure gradient ✔
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Option A: Lies above its centre of buoyancy
Option B: And centre of buoyancy coincide
Option C: Lies below its centre of buoyancy
Option D: Lies above its metacentre
Correct Answer: Lies below its centre of buoyancy ✔
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Option A: Angular velocity
Option B: Fanning friction factor
Option C: Specific volume
Option D: None of these
Correct Answer: Fanning friction factor ✔
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Option A: Linear with radius for turbulent flow only
Option B: Linear with radius for laminar flow only
Option C: Linear with radius for both laminar & turbulent flow
Option D: Parabolic with radius for both laminar & turbulent flow
Correct Answer: Linear with radius for both laminar & turbulent flow ✔
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The ratio of actual discharge to theoretical discharge through an orifice is equal to__________?
Option A: Cc . Cv
Option B: Cc . Cd
Option C: Cv . Cd
Option D: Cd/Cv
Correct Answer: Cc . Cv ✔
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Option A: Zero at the pipe wall and is a universal constant
Option B: Independent of radial distance from the pipe axis
Option C: Independent of the shear stress
Option D: Useful for computing laminar flow problems
Correct Answer: Useful for computing laminar flow problems ✔
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Option A: Placed farther from the wall
Option B: Not affected by other particles and the wall
Option C: Near each other
Option D: None of these
Correct Answer: Near each other ✔
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Option A: Normal
Option B: Local
Option C: Convective
Option D: Tangential
Correct Answer: Local ✔
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Option A: Cv . √(2gH)
Option B: Cc . √(2gH)
Option C: Cd . √(2gH)
Option D: Cv . Va
Correct Answer: Cv . √(2gH) ✔
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Option A: Pitot tube
Option B: Manometer
Option C: Rotameter
Option D: None of these
Correct Answer: Pitot tube ✔
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Option A: Inverse of the roughness
Option B: First power of the roughness
Option C: Square of the velocity
Option D: Inverse square of hydraulic radius
Correct Answer: First power of the roughness ✔
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Option A: Having high viscosities
Option B: Moving at low velocities
Option C: Both A. & B.
Option D: Neither A. nor B.
Correct Answer: C. Both A. & B. ✔
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Option A: Irrotational
Option B: Turbulent
Option C: Steady
Option D: None of these
Correct Answer: Irrotational ✔
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