Two jets
Two runners
Four jets
Four runners
B. Two runners
Centrifugal pump
Reciprocating pump
Jet pump
Air lift pump
Rotational flow
Radial
Forced spiral vortex flow
Spiral vortex flow
102 watts
75 watts
550 watts
735 watts
0 to 4.5
10 to 100
80 to 200
250 to 300
Designing new impeller
Trimming the impeller size to the required size by machining
Not possible
Some other alterations in the impeller
Slow speed pump with radial flow at outlet
Medium speed pump with radial flow at outlet
High speed pump with radial flow at outlet
High speed pump with axial flow at outlet
Directly as the air or gas density
Inversely as square root of density
Inversely as density
As square of density
Impeller diameter
Speed
Fluid density
Both (A) and (B) above
Straight
Bent forward
Bent backward
Radial
Two jets
Two runners
Four jets
Four runners
The water flows parallel to the axis of the wheel
The water enters at the centre of the wheel and then flows towards the outer periphery of the wheel
The water enters the wheel at the outer periphery and then flows towards the centre of the wheel
The flow of water is partly radial and partly axial
Ratio of the actual power produced by the turbine to the energy actually supplied by the turbine
Ratio of the actual work available at the turbine to the energy imparted to the wheel
Ratio of the Work done on the wheel to the energy of the jet
None of the above
Have identical velocities
Are equal in size and shape
Are identical in shape, but differ only in size
Have identical forces
Kinetic head
Velocity head
Manometric head
Static head
Directly as fan speed
Square of fan speed
Cube of fan speed
Square root of fan speed
At the top
At the bottom
At the canter
From sides
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
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
Have identical velocities
Are equal in size and shape
Are identical in shape, but differ only in size
Have identical forces
Same quantity of liquid
0.75 Q
Q/0.75
1.5 Q
Discharge a diameter
Head a speed²
Head a diameter
Power a speed⁴
waVr /g × (Vr + v)
waVr /g × (Vr - v)
waVr /g × (Vr + v)²
waVr /g × (Vr - v)²
0.15 to 0.3
0.4 to 0.5
0.6 to 0.9
1 to 1.5
High discharge
High head
Pumping of viscous fluids
High head and high discharge
2 to 4
4 to 8
8 to 16
16 to 24
Pelton wheel with one nozzle
Pelton wheel with two or more nozzles
Kaplan turbine
Francis turbine
Directly proportional
Inversely proportional
4th power
None of these
Centrifugal
Axial flow
Mixed flow
Reciprocating
Power produced by the turbine to the energy actually supplied by the turbine
Actual work available at the turbine to energy imparted to the wheel
Workdone on the wheel to the energy (or head of water) actually supplied to the turbine
None of the above
0.26
0.36
0.46
0.56