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Pump Basics
Centrifugal Pumps
From the Center
of a Circle
RADIAL DIRECTION
To the Outside of a Circle
A machine for moving fluid by accelerating the
fluid RADIALLY outward.
 This machine consists of an IMPELLER
rotating within a case (diffuser)
 Liquid directed into the
center of the rotating
impeller is picked up by
the impeller’s vanes and
accelerated to a higher velocity by the
rotation of the impeller and discharged by
centrifugal force into the case
(diffuser).
Centrifugal Pumps
Centrifugal Pumps
 A collection chamber in the casing converts
much of the Kinetic Energy (energy due to
velocity) into Head or Pressure.
Pump
Terminology
 Head is a term for expressing feet of water column
 Head can also be converted to pressure
"Head"
100
feet
43.3 PSI
Reservoir
of Fluid
Pressure
Gauge
Conversion Factors Between
Head and Pressure
 Head (feet of liquid) =Pressure in PSI x 2.31 / Sp. Gr.
 Pressure in PSI = Head (in feet) x Sp. Gr. / 2.31
 PSI is Pounds per Square Inch
 Sp. Gr. is Specific Gravity which for water is equal to
1
 For a fluid more dense than water, Sp. Gr. is
greater than 1
 For a fluid less dense than water, Sp. Gr. is less
than 1
Head
 Head and pressure are interchangeable
terms provided that they are expressed in
their correct units.
 The conversion of all pressure terms into
units of equivalent head simplifies most
pump calculations.
Diameter of
the Impeller
Thickness
of the impeller
Centrifugal Impellers
 Thicker the Impeller- More Water
 Larger the DIAMETER - More Pressure
 Increase the Speed - More Water and Pressure
Impeller
Vanes
“Eye of the
Impeller”
Water
Entrance
Two Impellers in Series
Direction of Flow
 Twice the pressure
 Same amount of water
Multiple Impellers in Series
 Placing impellers in series increases the amount of head
produced
 The head produced = # of impellers x head of one impeller
Direction of Flow Direction of Flow
Pump Performance Curve
 A mapping or graphing of the pump's ability to produce head
and flow
Pump Performance Curve
Step #1, Horizontal Axis
 The pump's flow rate is plotted on the horizontal axis ( X
axis)
 Usually expressed in Gallons per Minute
Pump Flow Rate
Pump Performance Curve
Step #2, Vertical Axis
Pump Flow Rate
 The head the pump produces is plotted on
the vertical axis (Y axis)
 Usually express in Feet of Water
Head
Pump Performance Curve
Step #3, Mapping the Flow and the Head
Pump Flow Rate
 Most pump
performance curves
slope from left to
right
Performance Curve
Head
Pump Performance Curve
Important Points
 Shut-off Head is the maximum pressure
or head the pump can produce
 No flow is produced
Pump Flow Rate
Head
Shut-off Head
Pump Performance Curve
Important Points
Pump Flow Rate
Head
Maximum Flow
 Maximum Flow is the
largest flow the pump can
produce
 No Head is produced
System Performance Curves
 System Performance Curve is a mapping
of the head required to produce flow in a
given system
 A system includes all the pipe, fittings and
devices the fluid must flow through, and
represents the friction loss the fluid
experiences
System Performance Curve
Step #1, Horizontal Axis
System Flow Rate
 The System's flow rate in plotted on the horizontal
axis ( X axis)
 Usually expressed in Gallons per Minute
System Performance Curve
Step #2, Vertical Axis
Pump Flow Rate
 The head the system requires is plotted on
the vertical axis (Y axis)
 Usually express in Feet of Water
Head
System Performance Curve
Step #3, Curve Mapping
 The friction loss is mapped onto the graph
 The amount of friction loss varies with flow through
the system
Head
Pump Flow Rate
Friction Loss
Head
Pump Flow Rate
The point on the system curve that intersects
the pump curve is known as the operating
point.
Head
Pump Flow Rate
Circulator 1
Circulator
2
Circulator 3
PUMP SELECTION
Controlling Pump Performance
 Changing the amount for friction loss or "Throttling the
Pump" will change the pump's performance
Head
Pump Flow Rate
PUMP SELECTION
Valve Open
Valve Partially Open
Valve Barely Open
Pump basicsPump basicsPump basicsPump basicsPump basics
Piping Design Equations
Heuristics for Pipe Diameter
0.494
0.408
0.343
3
:
2.607
:
1.065
,
,1000 /
, /
Liquids
w
D
Gases
w
D
D Diameter inches
w Mass Flowrate lb hr
Density lb ft



 
  
 
 
  
 



Energy Loss in Piping Networks
Incompressible Fluids
     
2 2
1 2 1 2 2 1
3
2
2
144 1
2
, /
, /
, /
, 32.174 /s
,
,
L
f
L
P P v v z z h
g
Density lb ft
P Pressure lb in
v Velocity ft sec
g Gravitational Acceleration ft
z Elevation ft
h Head loss ft


     






  2
4
2
2
1
2
2
0.00259
,
,
,
1 ,
L
K Q
h
d
Q Volumetric Flowrate gpm
d Pipe Diameter in
K Sum of all fittings
L
K f straight pipe
D
d
K Sudden enlargement
d





 
 
 
 


Friction Loss Factors for Fittings
Fitting K
Standard 90o
Elbow 30fT
Standard 45o
Elbow 16fT
Standard Tee
20fT Run
60 fT Branch
Pipe Entrance 0.78
Pipe Exit 1.0
Friction Loss Factors for Valves
Valve K
Gate valve 8fT
Globe Valve 340fT
Swing Check Valve 100fT
Lift Check Valve 600fT
Ball Valve 3fT
2
2
29.9
V
V
d
K
C
C Valve Coefficient


Fanning Diagram
f =16/Re

1
f
4.0 * log
D

 2.28

1
f
4.0 * log
D

 2.28  4.0 * log 4.67
D/
Re f
1






Energy Loss in Valves
 Function of valve type and valve
position
 The complex flow path through valves
can result in high head loss (of course,
one of the purposes of a valve is to
create head loss when it is not fully
open)
 Ev are the loss in terms of velocity
heads
Pump basicsPump basicsPump basicsPump basicsPump basics

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Pump basicsPump basicsPump basicsPump basicsPump basics

  • 2. Centrifugal Pumps From the Center of a Circle RADIAL DIRECTION To the Outside of a Circle A machine for moving fluid by accelerating the fluid RADIALLY outward.
  • 3.  This machine consists of an IMPELLER rotating within a case (diffuser)  Liquid directed into the center of the rotating impeller is picked up by the impeller’s vanes and accelerated to a higher velocity by the rotation of the impeller and discharged by centrifugal force into the case (diffuser). Centrifugal Pumps
  • 4. Centrifugal Pumps  A collection chamber in the casing converts much of the Kinetic Energy (energy due to velocity) into Head or Pressure.
  • 6.  Head is a term for expressing feet of water column  Head can also be converted to pressure "Head" 100 feet 43.3 PSI Reservoir of Fluid Pressure Gauge
  • 7. Conversion Factors Between Head and Pressure  Head (feet of liquid) =Pressure in PSI x 2.31 / Sp. Gr.  Pressure in PSI = Head (in feet) x Sp. Gr. / 2.31  PSI is Pounds per Square Inch  Sp. Gr. is Specific Gravity which for water is equal to 1  For a fluid more dense than water, Sp. Gr. is greater than 1  For a fluid less dense than water, Sp. Gr. is less than 1
  • 8. Head  Head and pressure are interchangeable terms provided that they are expressed in their correct units.  The conversion of all pressure terms into units of equivalent head simplifies most pump calculations.
  • 9. Diameter of the Impeller Thickness of the impeller Centrifugal Impellers  Thicker the Impeller- More Water  Larger the DIAMETER - More Pressure  Increase the Speed - More Water and Pressure Impeller Vanes “Eye of the Impeller” Water Entrance
  • 10. Two Impellers in Series Direction of Flow  Twice the pressure  Same amount of water
  • 11. Multiple Impellers in Series  Placing impellers in series increases the amount of head produced  The head produced = # of impellers x head of one impeller Direction of Flow Direction of Flow
  • 12. Pump Performance Curve  A mapping or graphing of the pump's ability to produce head and flow
  • 13. Pump Performance Curve Step #1, Horizontal Axis  The pump's flow rate is plotted on the horizontal axis ( X axis)  Usually expressed in Gallons per Minute Pump Flow Rate
  • 14. Pump Performance Curve Step #2, Vertical Axis Pump Flow Rate  The head the pump produces is plotted on the vertical axis (Y axis)  Usually express in Feet of Water Head
  • 15. Pump Performance Curve Step #3, Mapping the Flow and the Head Pump Flow Rate  Most pump performance curves slope from left to right Performance Curve Head
  • 16. Pump Performance Curve Important Points  Shut-off Head is the maximum pressure or head the pump can produce  No flow is produced Pump Flow Rate Head Shut-off Head
  • 17. Pump Performance Curve Important Points Pump Flow Rate Head Maximum Flow  Maximum Flow is the largest flow the pump can produce  No Head is produced
  • 18. System Performance Curves  System Performance Curve is a mapping of the head required to produce flow in a given system  A system includes all the pipe, fittings and devices the fluid must flow through, and represents the friction loss the fluid experiences
  • 19. System Performance Curve Step #1, Horizontal Axis System Flow Rate  The System's flow rate in plotted on the horizontal axis ( X axis)  Usually expressed in Gallons per Minute
  • 20. System Performance Curve Step #2, Vertical Axis Pump Flow Rate  The head the system requires is plotted on the vertical axis (Y axis)  Usually express in Feet of Water Head
  • 21. System Performance Curve Step #3, Curve Mapping  The friction loss is mapped onto the graph  The amount of friction loss varies with flow through the system Head Pump Flow Rate Friction Loss
  • 22. Head Pump Flow Rate The point on the system curve that intersects the pump curve is known as the operating point.
  • 23. Head Pump Flow Rate Circulator 1 Circulator 2 Circulator 3 PUMP SELECTION
  • 24. Controlling Pump Performance  Changing the amount for friction loss or "Throttling the Pump" will change the pump's performance
  • 25. Head Pump Flow Rate PUMP SELECTION Valve Open Valve Partially Open Valve Barely Open
  • 27. Piping Design Equations Heuristics for Pipe Diameter 0.494 0.408 0.343 3 : 2.607 : 1.065 , ,1000 / , / Liquids w D Gases w D D Diameter inches w Mass Flowrate lb hr Density lb ft                    
  • 28. Energy Loss in Piping Networks Incompressible Fluids       2 2 1 2 1 2 2 1 3 2 2 144 1 2 , / , / , / , 32.174 /s , , L f L P P v v z z h g Density lb ft P Pressure lb in v Velocity ft sec g Gravitational Acceleration ft z Elevation ft h Head loss ft              
  • 29.   2 4 2 2 1 2 2 0.00259 , , , 1 , L K Q h d Q Volumetric Flowrate gpm d Pipe Diameter in K Sum of all fittings L K f straight pipe D d K Sudden enlargement d               
  • 30. Friction Loss Factors for Fittings Fitting K Standard 90o Elbow 30fT Standard 45o Elbow 16fT Standard Tee 20fT Run 60 fT Branch Pipe Entrance 0.78 Pipe Exit 1.0
  • 31. Friction Loss Factors for Valves Valve K Gate valve 8fT Globe Valve 340fT Swing Check Valve 100fT Lift Check Valve 600fT Ball Valve 3fT 2 2 29.9 V V d K C C Valve Coefficient  
  • 32. Fanning Diagram f =16/Re  1 f 4.0 * log D   2.28  1 f 4.0 * log D   2.28  4.0 * log 4.67 D/ Re f 1      
  • 33. Energy Loss in Valves  Function of valve type and valve position  The complex flow path through valves can result in high head loss (of course, one of the purposes of a valve is to create head loss when it is not fully open)  Ev are the loss in terms of velocity heads