Two
Four
Six
Eight
C. Six
10° to 15°
15° to 20°
20° to 25°
25° to 30°
Speed and power developed
Discharge and power developed
Speed and head of water
Speed, power developed and head of water
Air lift pump
Jet pump
Hydraulic coupling
Hydraulic press
Accumulating oil
Supplying large quantities of oil for very short duration
Generally high pressures to operate hydraulic machines
Supplying energy when main supply fails
To store pressure energy which may be supplied to a machine later on
To increase the intensity of pressure of water by means of energy available from a large quantity of water at a low pressure
To lift larger load by the application of a comparatively much smaller force
All of the above
L.A.N
2 L.A.N
(L.A.N)/60
(2 L.A.N)/60
0.50 to 0.65
0.65 to 0.75
0.75 to 0.85
0.85 to 0.90
Installing the turbine below the tail race level
Using stainless steel runner of the turbine
Providing highly polished blades to the runner
All of the above
Normal speed
Unit speed
Specific speed
None of these
39.2 %
49.2 %
68.8 %
84.8 %
Radial
Axial
Centrifugal
Vortex
Medium head application from 24 to 180 m
Low head installation up to 30 m
High head installation above 180 m
All types of heads
To break the jet of water
To bring the runner to rest in a short time
To change the direction of runner
None of these
Suction lift + Loss of head in suction pipe due to friction + Delivery lift + Loss of head in delivery pipe due to friction + Velocity head in the delivery pipe
Workdone per kN of water Losses within the impeller
Energy per kN at outlet of impeller Energy per kN at inlet of impeller
All of the above
Rectilinear flow
Radial flow
Free vortex motion
Forced vortex
Delivers unit discharge under unit head
Delivers unit discharge under unit speed
Develops unit power under unit head
Develops unit power under unit speed
Casing
Delivery pipe
Suction pipe
Impeller
Kept fully closed
Kept fully open
Irrespective of any position
Kept 50% open
Directly proportional to N
Inversely proportional to N
Directly proportional to N²
Inversely proportional to N²
Have identical velocities
Are equal in size and shape
Are identical in shape, but differ only in size
Have identical forces
0.25 kW
0.75 kW
1.75 kW
3.75 kW
Slow speed with radial flow at outlet
Medium speed with radial flow at outlet
High speed with radial flow at outlet
High speed with mixed flow at outlet
Centrifugal pump
Axial flow pump
Mixed flow pump
Reciprocating pump
Energy available at the impeller to the energy supplied to the pump by the prime mover
Actual workdone by the pump to the energy supplied to the pump by the prime mover
Energy supplied to the pump to the energy available at the impeller
Manometric head to the energy supplied by the impeller per kN of water
N√P / H3/2
N√P / H²
N√P / H5/4
N√P / H3
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
Closed
Open
Depends on starting condition and flow desired
Could be either open or closed
Directly as fan speed
Square of fan speed
Cube of fan speed
Square root of fan speed
Product
Difference
Sum
None of these
Tangential flow impulse turbine
Inward flow impulse turbine
Outward flow impulse turbine
Inward flow reaction turbine