Impulse turbines
Reaction turbines
Axial flow turbines
Mixed flow turbines
B. Reaction turbines
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
40 %
50 %
60 %
80 %
Directly as the air or gas density
Inversely as square root of density
Inversely as density
As square of density
L.A.N
2 L.A.N
(L.A.N)/60
(2 L.A.N)/60
Centrifugal pump
Mixed flow pump
Axial flow pump
Any one of the above
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
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
Smoothen the flow
Reduce suction head
Increase delivery head
Reduce acceleration head
4
6
8
12
Propeller turbine
Francis turbine
Impulse turbine
None of the above
2 to 4
4 to 8
8 to 16
16 to 24
Discharge a diameter
Head a speed²
Head a diameter
Power a speed⁴
Friction loss
Cavitations
Static head
Loss of kinetic energy
An axial flow
An inward flow
An outward flow
A mixed flow
Same
0.75 B.H.P.
B.H.P./0.75
1.5 B.H.P.
At the top
At the bottom
At the canter
From sides
Directly proportional
Inversely proportional
4th power
None of these
No flow will take place
Cavitation will be formed
Efficiency will be low
Excessive power will be consumed
Pelton wheel
Francis turbine
Kaplan turbine
None of these
They have slow speeds
They are suitable even for low water heads
They give constant efficiency, even if the discharge is not constant
All of the above
Low head
High head
High head and low discharge
Low head and high discharge
Horizontal
Nearly horizontal
Steep
First rise and then fall
0.50 to 0.65
0.65 to 0.75
0.75 to 0.85
0.85 to 0.90
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
Tangential flow impulse turbine
Inward flow impulse turbine
Outward flow impulse turbine
Inward flow reaction turbine
Propeller turbine
Francis turbine
Impulse turbine
Any one of the above
Decreases
Increases
Remain same
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
24.8 r.p.m.
48.2 r.p.m
82.4 r.p.m.
248 r.p.m