Centrifugal pump
Mixed flow pump
Axial flow pump
Any one of the above
C. Axial flow pump
Delivers unit discharge under unit head
Delivers unit discharge under unit speed
Develops unit power under unit head
Develops unit power under unit speed
Strain
Pressure
Kinetic
None of these
High discharge
High head
Pumping of viscous fluids
High head and high discharge
Q = π.D.Vf
Q = π.b.Vf
Q = π.D.bf.V
Q = D.b.Vf
Pelton wheel
Kaplan turbine
Francis turbine
None of these
Impulse turbines
Reaction turbines
Axial flow turbines
Mixed flow turbines
N/√H
N/H
N/H3/2
N/H²
waV / 2g
waV / g
waV² / 2g
waV² / g
Medium head application from 24 to 180 m
Low head installation up to 30 m
High head installation above 180 m
All types of heads
Inlet of draft rube
Blade inlet
Guide blade
Penstock
(W/p) × (A/a)
(p/W) × (a/A)
(W/p) × (a/A)
(p/W) × (A/a)
At the level of tail race
Little above the tail race
Slightly below the tail race
About 2.5 m above the tail race to avoid cavitations.
High initial and maintenance cost
Lower discharge
Lower speed of operation
Necessity of air vessel
To store pressure energy which may be supplied to a machine later on
To increase the intensity of pressure of water by means of energy available from a large quantity of water at a low pressure
To lift larger load by the application of a comparatively much smaller force
All of the above
One-fourth
One-half
Three-fourth
Double
Adjustable blades
Backward curved blades
Vaned diffusion casing
Inlet guide blades
Product
Difference
Sum
None of these
Volute casing
Volute casing with guide blades
Vortex casing
Any one of these
Sum
Difference
Product
None of these
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
Designing new impeller
Trimming the impeller size to the required size by machining
Not possible
Some other alterations in the impeller
Screw pump
Gear pump
Cam and piston pump
Plunger pump
Potential Energy
Strain Energy
Kinetic energy
None of these
Equal to
1.2 times
1.8 times
Double
Lift and resultant force
Drag and resultant force
Lift and tangential force
Lift and drag
Directly proportional to H1/2
Inversely proportional to H1/2
Directly proportional to H3/2
Inversely proportional to H3/2
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
Propeller turbine
Francis turbine
Impulse turbine
Any one of the above
Rectilinear flow
Radial flow
Free vortex motion
Forced vortex
Closed
Open
Depends on starting condition and flow desired
Could be either open or closed