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CENTRIFUGAL PUMP
MAJOR
ASSIGNMENT
SUBMITTED By:
BRIJESH KUMAR
UID-K10668
BRANCH – MECHANICAL(6-
SEM)
SUBMITTED TO :
MR.ADITYA MISRA
WHAT IS CENTRIFUGAL PUMP?
WORKING MECHANISM OF A
CENTRIFUGAL PUMP
ADVANTEGAES AND
DISADVANTAGES OF
CENTRIFUGAL PUMPS
Centrifugal pump works on the principle that
when a certain mass of liquid is made to rotate
along the impeller from the central axis of rotation,
it impresses a centrifugal head. It causes the water
to move radially outwards at higher velocity and
causes the water to rise to a higher level. The
motion of water is restricted by casing of pump, it
result into pressure build up. In addition , the
change in angular momentum of liquid during its
fiow reults into increase in pressure head.
The steps involved in operation of centrifugal
pump are as follows :
1.The delivery valve is closed.
2.The priming of the pump is carried out. Priming
involves the filling the liquid in suction pipe and
casing upto the level of delivery valve so that no air
pockets are left in the system.
if any air or gas pockets are left in this portion of
pump, it may result into no delivery of liquid by
the pump.
3. The pump shaft and impeller is now rotated
with the help of an external source of power
like a motor or any other prime mover.
The rotation of impeller inside a casing full
of liquid produces a forced vortex which is
responsible in imparting the centrifugal head
to the liquid. It creates a vaccum at the eye of
impeller and causes liquid to rise into suction
pipe from the sump.
4. The speed of impeller should be sufficient to
produce the centrifugal head such that it can
initiate discharge from delivery pipe.
5. Now the delivery valve is opened and the
liquid is lifted and discharge through the
delivery pipe due to its high pressure.
Thus the liquid is continously sucked from
the sump to impeller eye and it is delivered
from the casing of pump through the delivery
pipe.
6. Before stopping the pump, it is necessary to
close the delivery pipe otherwise the back
flow of liquid may take place from the high
head reservoir.
:- In case the priming of pump is not
done and the pump is not done and the
pump is not under the operation, the
water present in the pump and suction
pipe will flow back to the sump. The space
occupied by water will be filled by air.
:- The operation of filling the casing ,
impeller and suction pipe and the
portion of delivery pump upto delivery
valve is called priming.
:- If the pump is now started, the air
pockets inside the impeller may give
rise to vortices and cause the
discontinuity of flow. Under these
condition, the flow of fluid does not
commence and the pump runs dry. It
causes the rubbing and seizing of the
wearing rings, increases noise level and
vibrations and finally may cause the
serious damage to pump.
:- The priming in resiprocating
pumps is not required since the
pumping is done by positively moving
the fluid out of the cylinder by the
piston. Hence, the air will be displaced
from the casing when the pump starts
and it will get a suction pressure which
will draw the fluid from the sump.
Priming for small pumps is done
by hand
:- A foot valve is essential at the
bottom of suction pipe
:- A funnel or priming cup is
provided to fill the water by hand.
An air vent is provided in the
casing of pump. When the water
is filled, the air escapes through
the air vent. It is closed once the
priming is completed
Convert the mechanical
energy into hydraulic
energy by centrifugal
force on the liquid
Constitute the most
common type of
pumping machinery
Used to move liquids
through a piping system
Has two main
components:
1. Stationary componets,
casing, casing cover and
bearings
2. Rotating components,
impeller and shaft
Classified into three
categories ; Radial Flow,
Mixed Flow, Axial Flow
Simplest piece of
equipment in any process
plant
Energy changes occur by
virtue of impeller and
volute
Liquid is fed into the
pump at the center of a
rotating impeller and
thrown outward by
centrifugal force
The conversion of kinetic
energy into pressure
energy supplies the
pressure difference
between the suction side
and delivery side of the
pump
Liquid flow path
inside a
centrifugal pump
•The power supplied to the pump:
Where m=mass flow rate, kg/s
∆H= total discharge head,
N.m/kg
η=efficiency
…………(1)
•The power delivered to the fluid:
…………(2)
•From equations (1) and (2)
efficiency:
nq is the specific speed for a unit
machine that is geometric similar to a
machine with the head Hq = 1 m and
flow rate Q = 1 m3
/s
43q
H
Q
nn ⋅=
qs nn ⋅= 55,51
Three basic
components:
Volute, casing,
body
or Diffuser
Impeller
or impellers
Driver (motor)
Centrifugal Pumps
Vanes
Direction of
rotation
Centrifugal Pumps
Single suction impeller
Centrifugal Pumps
• Open
• Semi-open
• Closed
- Single suction
- Double suction
• Non-clogging
• Axial flow
• Mixed flow
Maximum efficiency lies
in the range:
2000<NS<3000
High head, low capacity
pumps:
500<NS<1000
Low head, large capacity
pumps:
NS>15000
Centrifugal Pumps
Rotation
Impeller
Blades
Vt
V
r
V
s
Vr = Radial Velocity
Vt = Tangential Velocity
Vs = Vector Sum Velocity
Centrifugal Pumps
Suction Eye
Cutwater
Arrows represent the
direction of water flow
Discharge
Nozzle
Advantages
Simple in construction
and cheap
Handle liquid with large
amounts of solids
No metal to metal fits
No valves involved in
pump operation
Maintenance costs are
lower
Disadvantages
Cannot handle highly viscous
fluids efficiently
Cannot be operated at high
heads
Maximum efficiency holds
over a narrow range of
conditions
Centrifugal Pump Major Assignment

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Centrifugal Pump Major Assignment

  • 1. CENTRIFUGAL PUMP MAJOR ASSIGNMENT SUBMITTED By: BRIJESH KUMAR UID-K10668 BRANCH – MECHANICAL(6- SEM) SUBMITTED TO : MR.ADITYA MISRA
  • 2. WHAT IS CENTRIFUGAL PUMP? WORKING MECHANISM OF A CENTRIFUGAL PUMP ADVANTEGAES AND DISADVANTAGES OF CENTRIFUGAL PUMPS
  • 3. Centrifugal pump works on the principle that when a certain mass of liquid is made to rotate along the impeller from the central axis of rotation, it impresses a centrifugal head. It causes the water to move radially outwards at higher velocity and causes the water to rise to a higher level. The motion of water is restricted by casing of pump, it result into pressure build up. In addition , the change in angular momentum of liquid during its fiow reults into increase in pressure head. The steps involved in operation of centrifugal pump are as follows : 1.The delivery valve is closed. 2.The priming of the pump is carried out. Priming involves the filling the liquid in suction pipe and casing upto the level of delivery valve so that no air pockets are left in the system. if any air or gas pockets are left in this portion of pump, it may result into no delivery of liquid by the pump.
  • 4. 3. The pump shaft and impeller is now rotated with the help of an external source of power like a motor or any other prime mover. The rotation of impeller inside a casing full of liquid produces a forced vortex which is responsible in imparting the centrifugal head to the liquid. It creates a vaccum at the eye of impeller and causes liquid to rise into suction pipe from the sump. 4. The speed of impeller should be sufficient to produce the centrifugal head such that it can initiate discharge from delivery pipe. 5. Now the delivery valve is opened and the liquid is lifted and discharge through the delivery pipe due to its high pressure. Thus the liquid is continously sucked from the sump to impeller eye and it is delivered from the casing of pump through the delivery pipe. 6. Before stopping the pump, it is necessary to close the delivery pipe otherwise the back flow of liquid may take place from the high head reservoir.
  • 5. :- In case the priming of pump is not done and the pump is not done and the pump is not under the operation, the water present in the pump and suction pipe will flow back to the sump. The space occupied by water will be filled by air. :- The operation of filling the casing , impeller and suction pipe and the portion of delivery pump upto delivery valve is called priming.
  • 6. :- If the pump is now started, the air pockets inside the impeller may give rise to vortices and cause the discontinuity of flow. Under these condition, the flow of fluid does not commence and the pump runs dry. It causes the rubbing and seizing of the wearing rings, increases noise level and vibrations and finally may cause the serious damage to pump. :- The priming in resiprocating pumps is not required since the pumping is done by positively moving the fluid out of the cylinder by the piston. Hence, the air will be displaced from the casing when the pump starts and it will get a suction pressure which will draw the fluid from the sump.
  • 7. Priming for small pumps is done by hand :- A foot valve is essential at the bottom of suction pipe :- A funnel or priming cup is provided to fill the water by hand. An air vent is provided in the casing of pump. When the water is filled, the air escapes through the air vent. It is closed once the priming is completed
  • 8. Convert the mechanical energy into hydraulic energy by centrifugal force on the liquid Constitute the most common type of pumping machinery Used to move liquids through a piping system Has two main components: 1. Stationary componets, casing, casing cover and bearings 2. Rotating components, impeller and shaft Classified into three categories ; Radial Flow, Mixed Flow, Axial Flow
  • 9. Simplest piece of equipment in any process plant Energy changes occur by virtue of impeller and volute Liquid is fed into the pump at the center of a rotating impeller and thrown outward by centrifugal force The conversion of kinetic energy into pressure energy supplies the pressure difference between the suction side and delivery side of the pump Liquid flow path inside a centrifugal pump
  • 10. •The power supplied to the pump: Where m=mass flow rate, kg/s ∆H= total discharge head, N.m/kg η=efficiency …………(1)
  • 11. •The power delivered to the fluid: …………(2) •From equations (1) and (2) efficiency:
  • 12. nq is the specific speed for a unit machine that is geometric similar to a machine with the head Hq = 1 m and flow rate Q = 1 m3 /s 43q H Q nn ⋅= qs nn ⋅= 55,51
  • 13. Three basic components: Volute, casing, body or Diffuser Impeller or impellers Driver (motor)
  • 16. Centrifugal Pumps • Open • Semi-open • Closed - Single suction - Double suction • Non-clogging • Axial flow • Mixed flow
  • 17. Maximum efficiency lies in the range: 2000<NS<3000 High head, low capacity pumps: 500<NS<1000 Low head, large capacity pumps: NS>15000
  • 18. Centrifugal Pumps Rotation Impeller Blades Vt V r V s Vr = Radial Velocity Vt = Tangential Velocity Vs = Vector Sum Velocity
  • 19. Centrifugal Pumps Suction Eye Cutwater Arrows represent the direction of water flow Discharge Nozzle
  • 20. Advantages Simple in construction and cheap Handle liquid with large amounts of solids No metal to metal fits No valves involved in pump operation Maintenance costs are lower
  • 21. Disadvantages Cannot handle highly viscous fluids efficiently Cannot be operated at high heads Maximum efficiency holds over a narrow range of conditions

Editor's Notes

  1. A