Directly proportional to diameter of its impeller
Inversely proportional to diameter of its impeller
Directly proportional to (diameter)² of its impeller
Inversely proportional to (diameter)² of its impeller
D. Inversely proportional to (diameter)² of its impeller
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
2 to 4
4 to 8
8 to 16
16 to 24
Strain
Pressure
Kinetic
None of these
Q = π.D.Vf
Q = π.b.Vf
Q = π.D.bf.V
Q = D.b.Vf
Centrifugal
Axial flow
Mixed flow
Reciprocating
Centrifugal pump
Mixed flow pump
Axial flow pump
None of the above
N√P / H3/2
N√P / H²
N√P / H5/4
N√P / H3
Geometric similarity
Kinematic similarity
Dynamic similarity
None of these
Straight
Bent forward
Bent backward
Radial
Girad turbine
Turgo turbine
Pelton wheel
Kaplan turbine
Pelton wheel
Kaplan turbine
Francis turbine
None of these
Fourneyron turbine
Journal turbine
Thomson's turbine
Pelton wheel
Propeller turbine
Francis turbine
Impulse turbine
Any one of the above
0.15 to 0.3
0.4 to 0.5
0.6 to 0.9
1 to 1.5
Velocity of flow at inlet to the theoretical jet velocity
Theoretical velocity of jet to the velocity of flow at inlet
Velocity of runner at inlet to the velocity of flow at inlet
None of the above
Friction loss
Cavitations
Static head
Loss of kinetic energy
ηh = ηo × ηm
ηm = ηm × ηh
ηo = ηh × ηm
None of these
To run the turbine full
To prevent air to enter the turbine
To increase the head of water by an amount equal to the height of the runner outlet above the tail race
To transport water to downstream
24.8 r.p.m.
48.2 r.p.m
82.4 r.p.m.
248 r.p.m
Slow speed with radial flow at outlet
Medium speed with radial flow at outlet
High speed with radial flow at outlet
High speed with mixed flow at outlet
Centrifugal pump
Reciprocating pump
Jet pump
Airlift pump
(1 + cos φ)/2
(1 - cos φ)/2
(1 + sin φ)/2
(1 - sin φ)/2
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
Have identical velocities
Are equal in size and shape
Are identical in shape, but differ only in size
Have identical forces
[2(Vr - v) v]/ Vr²
2(Vr + v) v]/ Vr²
[(Vr - v) v]/ Vr
[(Vr + v) v]/ Vr
Impeller diameter
Speed
Fluid density
Both (A) and (B) above
waV / 2g
waV / g
waV² / 2g
waV² / g
Hydraulic ram
Hydraulic intensifier
Hydraulic torque converter
Hydraulic accumulator
An axial flow
An inward flow
An outward flow
A mixed flow
Sum
Difference
Product
None of these