39.2 %
48.8 %
84.8 %
88.4 %
A. 39.2 %
Have identical velocities
Are equal in size and shape
Are identical in shape, but differ only in size
None of the above
Low head
High head
High head and low discharge
Low head and high discharge
24.8 r.p.m.
48.2 r.p.m
82.4 r.p.m.
248 r.p.m
175.4 r.p.m.
215.5 r.p.m.
241.5 r.p.m.
275.4 r.p.m
Same quantity of liquid
0.75 Q
Q/0.75
1.5 Q
Horizontal
Nearly horizontal
Steep
First rise and then fall
Equal to
1.2 times
1.8 times
Double
Increases with increase in pressure
Decreases with increase in pressure
More or less remains constant with increase in pressure
Unpredictable
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
Q/√H
Q/H
Q/H3/2
Q/H²
Have identical velocities
Are equal in size and shape
Are identical in shape, but differ only in size
Have identical forces
Radially, axially
Axially, radially
Axially, axially
Radially, radially
Girad turbine
Turgo turbine
Pelton wheel
Kaplan turbine
Impeller diameter
Speed
Fluid density
Both (A) and (B) above
No flow will take place
Cavitation will be formed
Efficiency will be low
Excessive power will be consumed
(N√Q)/H2/3
(N√Q)/H3/4
(N√Q)/H
(N√Q)/H5/4
10° to 15°
15° to 20°
20° to 25°
25° to 30°
0.25 m3/s
0.5 m3/s
1.5 m3/s
2.5 m3/s
Centrifugal pump
Reciprocating pump
Jet pump
Air lift pump
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
Ratio of actual discharge to the theoretical discharge
Sum of actual discharge and the theoretical discharge
Difference of theoretical discharge and the actual discharge
Product of theoretical discharge and the actual discharge
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
Manometric efficiency
Mechanical efficiency
Overall efficiency
Volumetric efficiency
Centrifugal pump
Axial flow pump
Mixed flow pump
Reciprocating pump
Geometric similarity
Kinematic similarity
Dynamic similarity
None of these
Kept fully closed
Kept fully open
Irrespective of any position
Kept 50% open
39.2 %
49.2 %
68.8 %
84.8 %
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
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
High initial and maintenance cost
Lower discharge
Lower speed of operation
Necessity of air vessel