Fourneyron turbine
Journal turbine
Thomson's turbine
Pelton wheel
D. Pelton wheel
Power produced by the turbine to the energy actually supplied by the turbine
Actual work available at the turbine to the 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
ηh = ηo × ηm
ηm = ηm × ηh
ηo = ηh × ηm
None of these
Casing
Delivery pipe
Suction pipe
Impeller
Net head
Absolute velocity
Blade velocity
Flow
10-15°
20-25°
30-40°
50-60°
At the top
At the bottom
At the canter
From sides
Propeller turbine
Francis turbine
Impulse turbine
Any one 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
Slow speed with radial flow at outlet
Medium speed with radial flow at outlet
High speed with radial flow at outlet
High speed with axial flow at outlet
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
Directly as the air or gas density
Inversely as square root of density
Inversely as density
As square of density
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
[wa (V - v)]/2g
[wa (V - v)]/g
[wa (V - v)²]/2g
[wa (V - v²)]/g
Pelton wheel
Kaplan turbine
Francis turbine
None of these
Radially, axially
Axially, radially
Axially, axially
Radially, radially
Hydraulic
Mechanical
Overall
None of these
Directly as the air or gas density
Inversely as square root of density
Inversely as density
As square of density
Closed
Open
Depends on starting condition and flow desired
Could be either open or closed
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
Lift and resultant force
Drag and resultant force
Lift and tangential force
Lift and drag
0.15 to 0.3
0.4 to 0.5
0.6 to 0.9
1 to 1.5
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
0.25 kW
0.75 kW
1.75 kW
3.75 kW
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
Have identical velocities
Are equal in size and shape
Are identical in shape, but differ only in size
Have identical forces
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
Q = π.D.Vf
Q = π.b.Vf
Q = π.D.bf.V
Q = D.b.Vf
Directly as fan speed
Square of fan speed
Cube of fan speed
Square root of fan speed
Girad turbine
Turgo turbine
Pelton wheel
Kaplan turbine
Low head of water
High head of water
Medium head of water
High discharge