A. Paddle

B. All A., B. and C.

C. Turbine

A. Remain same

B. Decrease

D. Data insufficient to predict pressure drop

B. Along which a fluid particle travels

C. None of these

D. That is traced by all the fluid particles passing through a given point

A. Vibratory

B. Elastic

C. Centrifugal

A. Dependent on the speed of the pump

B. 150 feet

D. Dependent on the power of the pump

A. Inverse square of hydraulic radius

B. Inverse of the roughness

C. Square of the velocity

B. Bottom plate moving and the top plate fixed

C. Both the plates fixed

D. Both the plates moving

A. Sub-atmospheric pressure

C. Atmospheric pressure

D. None of these

A. Expanding tube at increasing rate

B. Long pipe at constant rate

D. Long pipe at decreasing rate

A. 1

C. 0.5

D. 1.5

A. Gas turbine

B. Steam

C. Diesel engine

A. d2

B. d1/3

C. d2/3

B. Diffuser

C. Turbine

D. None of these

A. 2

C. 2-Jan

A. Wall roughness

B. Reynolds number

D. Neither A. nor B.

B. Mixes the two fluids before pumping them

C. Pumps the two fluids separately and then mixes them

D. Employs impellers in both the radial & axial directions

B. Newtonian

C. Dilatant

D. Pseudo-plastic

A. Drag = buoyancy + weight

B. Buoyancy = weight + drag

C. Drag = weight

A. Either open or closed

B. None of these

C. Closed

A. Decreases and then increases

B. Remains constant

D. Increases and then decreases

A. 45 and 60

B. 90 and 80

D. 20 and 120

A. Having high viscosities

B. Moving at low velocities

D. Neither A. nor B.

A. Elastic

C. Gravity

D. Viscous

A. Semi-circle

B. Semi-ellipse

C. Hyperbola

A. Flanges

B. Welding

D. Soldering

A. Reduce the cost of compressor

C. Reduce the size requirement

D. Are easy to control

A. H5/2

B. H2/5

C. H1/2

A. Static submergence

B. Priming

D. Cavitation sensitivity

A. Streamline

B. Creep

C. Boundary layer

A. Momentum transfer is on molecular scale only

B. Fluid particles move in an orderly manner

D. Shear stress is caused more effectively by cohesion than momentum transfer

B. Impeller diameter or speed

C. Number of pumps and joining them in series

D. Number of pumps and joining them in parallel

A. Requires more power

B. Capacity is reduced

D. Develops a lower head

A. It is not very accurate

C. It is very costly

D. It is not suitable for measuring gas flow

A. Euler

B. Reynolds

C. Weber

B. 1

C. 50

D. > 3

A. 5 kg/m3

B. 0 N/m

C. 1 N

A. Viscous fluid flow between converging plates

B. Fluid flow between parallel plates

C. None of these

A. Increases

B. May increase or decrease; depends on the magnitude of shear rate

D. Remain same

B. L2T

C. MLT-1

D. L2T-2

B. Surface tension of the liquid

C. Viscosity of the liquid

D. Depth of immersion of the body

A. Less

C. Unpredictable

D. Same

A. V

B. 1/V

D. 1/V2

A. Length is shorter

B. Throat diameter is more

D. Distance between the throat and the inlet is more

A. None of these

B. Pressure increase due to closure of a valve resulting in decrease in rate of flow

D. Bursting of pipelines due to closure by a valve

A. Measured normal to the channel bed

B. None of these

C. Corresponding to steady flow

A. Steady flow

B. Laminar flow through an open channel

D. Turbulent flow

A. Change in pressure

C. Change in total energy

D. Change in direction of flow

A. Ideal plastic

C. None of these

D. Dilatent fluid

A. Is zero at the plates and increases linearly to the mid-plane

B. None of these

D. Is constant over the entire cross-section

B. Dynamic

C. Static

D. Total