Centrifugal pump
Mixed flow pump
Axial flow pump
None of the above
A. Centrifugal pump
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
At the top
At the bottom
At the canter
From sides
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
[2(Vr - v) v]/ Vr²
2(Vr + v) v]/ Vr²
[(Vr - v) v]/ Vr
[(Vr + v) v]/ Vr
175.4 r.p.m.
215.5 r.p.m.
241.5 r.p.m.
275.4 r.p.m
Low head
High head
High head and low discharge
Low head and high discharge
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
Give high discharge
Produce high heads
Pump viscous fluids
All of these
Diameter
Square of diameter
Cube of diameter
Fourth power of diameter
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
Rotational flow
Radial
Forced spiral vortex flow
Spiral vortex flow
Net head
Absolute velocity
Blade velocity
Flow
(N√Q)/H2/3
(N√Q)/H3/4
(N√Q)/H
(N√Q)/H5/4
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
Suction pipe is short and pump is running at low speeds
Delivery pipe is long and pump is running at high speeds
Suction pipe is short and delivery pipe is long and the pump is running at low speeds
Suction pipe is long and delivery pipe is short and the pump is running at high speeds
Diameter of jet to the diameter of Pelton wheel
Velocity of jet to the velocity of Pelton wheel
Diameter of Pelton wheel to the diameter of jet
Velocity of Pelton wheel to the velocity of jet
Friction loss
Cavitations
Static head
Loss of kinetic energy
One-fourth
One-half
Three-fourth
Double
Smoothen the flow
Reduce suction head
Increase delivery head
Reduce acceleration head
Girad turbine
Turgo turbine
Pelton wheel
Kaplan turbine
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
(D/2d) + 5
(D/2d) + 10
(D/2d) + 15
(D/2d) + 20
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
Pelton wheel
Kaplan turbine
Francis turbine
None of these
2 to 4
4 to 8
8 to 16
16 to 24
Centrifugal pump
Axial flow pump
Mixed flow pump
Reciprocating pump
10 r.p.m.
20 r.p.m.
40 r.p.m.
80 r.p.m.
Directly as the air or gas density
Inversely as square root of density
Inversely as density
As square of density
[wa (V - v)]/2g
[wa (V - v)]/g
[wa (V - v)²]/2g
[wa (V - v²)]/g
Same
0.75 B.H.P.
B.H.P./0.75
1.5 B.H.P.