Low head of water
High head of water
Medium head of water
High discharge
B. High head of water
Centrifugal
Axial flow
Reciprocating
Mixed flow
Normal speed
Unit speed
Specific speed
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
2 to 4
4 to 8
8 to 16
16 to 24
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
0 to 4.5
10 to 100
80 to 200
250 to 300
An axial flow
An inward flow
An outward flow
A mixed flow
ηh = ηo × ηm
ηm = ηm × ηh
ηo = ηh × ηm
None of these
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
Two
Four
Six
Eight
Horizontal
Nearly horizontal
Steep
First rise and then fall
2 to 4
4 to 8
8 to 16
16 to 24
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
Two cylinders, two rams and a storage device
A cylinder and a ram
Two coaxial rams and two cylinders
A cylinder, a piston, storage tank and control valve
Radially, axially
Axially, radially
Axially, axially
Radially, radially
Adjustable blades
Backward curved blades
Vaned diffusion casing
Inlet guide blades
[wa (V - v)]/2g
[wa (V - v)]/g
[wa (V - v)²]/2g
[wa (V - v²)]/g
Flow vs. swept volume
Pressure in cylinder vs. swept volume
Flow vs. speed
Pressure vs. speed
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
Centrifugal pump
Reciprocating pump
Jet pump
Air lift pump
Casing
Delivery pipe
Suction pipe
Impeller
An axial flow
An inward flow
An outward flow
A mixed flow
Friction loss
Cavitations
Static head
Loss of kinetic energy
Of such a size that it delivers unit discharge at unit head
Of such a size that it delivers unit discharge at unit power
Of such a size that it requires unit power per unit head
Of such a size that it produces unit horse power with unit head
No flow will take place
Cavitation will be formed
Efficiency will be low
Excessive power will be consumed
Directly as the air or gas density
Inversely as square root of density
Inversely as density
As square of density
Centrifugal pump
Mixed flow pump
Axial flow pump
Any one of the above
Geometric similarity
Kinematic similarity
Dynamic similarity
None of these
waVr /g × (Vr + v)
waVr /g × (Vr - v)
waVr /g × (Vr + v)²
waVr /g × (Vr - v)²
Sum
Difference
Product
None of these