Equal to
1.2 times
1.8 times
Double
B. 1.2 times
N√P / H3/2
N√P / H²
N√P / H5/4
N√P / H3
Ratio of diameters
Square of ratio of diameters
Inverse ratio of diameters
Square of inverse ratio of diameters
Discharge a diameter
Head a speed²
Head a diameter
Power a speed⁴
Directly proportional to diameter of its impeller
Inversely proportional to diameter of its impeller
Directly proportional to (diameter)² of its impeller
Inversely proportional to (diameter)² of its impeller
0.50 to 0.65
0.65 to 0.75
0.75 to 0.85
0.85 to 0.90
Impulse turbines
Reaction turbines
Axial flow turbines
Mixed flow turbines
Directly as fan speed
Square of fan speed
Cube of fan speed
Square root of fan speed
waV / 2g
waV / g
waV² / 2g
waV² / g
Friction loss
Cavitations
Static head
Loss of kinetic energy
Impeller diameter
Speed
Fluid density
Both (A) and (B) above
Two
Four
Six
Eight
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
Greater than 15°
Greater than 8°
Greater than 5°
Less than 8°
Radial
Axial
Centrifugal
Vortex
Slow speed with radial flow at outlet
Medium speed with radial flow at outlet
High speed with radial flow at outlet
High speed with axial flow at outlet
Decreases
Increases
Remain same
None of these
An axial flow
An inward flow
An outward flow
A mixed flow
2 to 4
4 to 8
8 to 16
16 to 24
One-half
One-third
Two-third
Three-fourth
40 %
50 %
60 %
80 %
Designing new impeller
Trimming the impeller size to the required size by machining
Not possible
Some other alterations in the impeller
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
10° to 15°
15° to 20°
20° to 25°
25° to 30°
The centrifugal pump is suitable for large discharge and smaller heads.
The centrifugal pump requires less floor area and simple foundation as compared to reciprocating pump.
The efficiency of centrifugal pump is less as compared to reciprocating pump.
All of the above
Full load speed
The speed at which turbine runner will be damaged
The speed if the turbine runner is allowed to revolve freely without load and with the wicket gates wide open
The speed corresponding to maximum overload permissible
Product
Difference
Sum
None of these
Centrifugal
Axial flow
Mixed flow
Reciprocating
Allow the water to enter the runner without shock
Allow the water to flow over them, without forming eddies
Allow the required quantity of water to enter the turbine
All of the above
Double
Three times
Four times
Five times
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2