Transcript Document

Pumps
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Outline:
Where are pumps used
Pumps, fans, compressor differences
General HP and mechanical efficiency
Types of Pumps
– Displacement
– Dynamic
• Reading:
– Handouts:
• Chapter 4 Principles of Process Engineering
• Fluide Design Inc. Centrifugal Pump Fundamentals (download)
Dr. C. L. Jones
Biosystems and Ag. Engineering
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Pumps, Fans, Compressors-Turbomachines
• Turbomachines: change energy level of flowing fluid
by means of momentum exchange
• 2nd only to electric motors in number
• Wide spread in ALL industries
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Power units: cars/trucks, tractors
Computers
Grain elevators
Oilfield
Water supply/treatment
Food processing
And…….
Dr. C. L. Jones
Biosystems and Ag. Engineering
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Pumps, Fans, Compressors-Turbomachines
• Differences between pumps, fans,
compressors
– Pumps: move liquids
– Fans: move gases with little increase in
pressure
– Compressors: move gases with greater
increase in pressure
Dr. C. L. Jones
Biosystems and Ag. Engineering
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Mechanical Efficiency
PowerOutput
PowerInput
• Ratio:
• Power Output: Po  WQ g
• English Units, HP:
• Efficiency
Po 
QP
1714
Po
em 
Pi
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Biosystems and Ag. Engineering
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Pump example 1
• A pump provides 0.009 m^3/s of water
and total head of 10.6 m. Determine
the power output of the pump. If the
power input is 1310 W, determine the
mechanical efficiency of the pump.
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Pumps
• Two types
Flow rates
Pressure
Flow
characteristics
Displacement
- plunger
- piston
- rotary
Low
High
Pulsating
Dynamic
- centrifugal
- jet
- airlift
High
Low
Steady Flow
Dr. C. L. Jones
Biosystems and Ag. Engineering
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Displacement Pumps
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Biosystems and Ag. Engineering
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Displacement Pumps
• Reciprocating and Piston Pumps
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Crank
Connecting rods
Pistons or plungers
Vol. efficiencies > 97%, Mech. eff. approx. 90%
For more stable flow, increase number of
cylinders
Dr. C. L. Jones
Biosystems and Ag. Engineering
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Displacement Pumps
• Rotary Pumps (gear, lobe, screw, vane)
– Most popular: gear pumps
– 90%+ mechanical eff.
– Relatively constant output
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Biosystems and Ag. Engineering
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Dynamic Pumps
• Centrifugal
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Relative simplicity
Mech. eff. as high as 90%
Can handle fluids containing suspended solids
Ease of maintenance…good for food products
2 parts: impeller and casing
Radial, mixed, axial flow
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Performance Curves
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Performance Curves
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Centrifugal Pump Affinity Laws
Q1  N1  D1 

 
Q2  N2  D2 
3
2
W1  N1   D1 
   
W2  N2   D2 
3
2
5
Po1  N1   D1   1 
     
Po 2  N2   D2   2 
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Centrifugal Pump Affinity Laws
300  1750  13" 


Q2  2000 
13"


1601  1750 


W2  2000 
20  1750 

Po 2  2000 
3
2
3
 13 
 13 
 
2
5
 13 
 13  1
 
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Biosystems and Ag. Engineering
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Centrifugal Pump Fundamentals
• Static head: the height of a column of liquid
– Units: feet or meters
• Pump imparts velocity to liquid…velocity
energy becomes pressure energy leaving
the pump. Head developed = vel. energy at
the impeller tips. H  v 2 v  rpm  D
2g
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• Why do we use “feet” or “head” instead of
“psi” or “pressure”?
– Pump with impeller D will raise a liquid to a
certain height regardless of weight of liquid
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Biosystems and Ag. Engineering
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Converting pressure to head in feet
head, ft 
2.31 Psurface  Pvapor 
specific gravity
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Suction Lift
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Suction Head
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Static Discharge Head
• Static Discharge Head = vertical distance
from pump centerline to the point of free
discharge or the surface of the liquid in the
discharge tank.
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Total Static Head
• Vertical distance between the free level of
the source of supply and the point of free
discharge or the free surface of the
discharge liquid.
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Total Dynamic Suction Lift or
Head
• (fluid below suction) Static suction lift velocity head at suction + total friction head
in suction line
• (fluid above suction) Static suction head +
velocity head at pump suction flange – total
friction head in suction line
• Velocity head = energy of liquid due to
motion, Usually insignificant h  v 2
v
2g
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Biosystems and Ag. Engineering
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Total Dynamic Discharge Head
• Static discharge head + velocity head at
pump discharge flange plus discharge line
friction
Total Dynamic Discharge Head
(TH or TDH) (this is what we design for!!!)
• Total dynamic discharge head – total
dynamic suction head (tank above
suction)…. Or….
• Total dynamic discharge head + total
dynamic suction lift (tank below suction)
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Total Dynamic Discharge Head
(TH or TDH) (this is what we design for!!!)
TDH includes friction losses due to
piping and velocity
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Biosystems and Ag. Engineering
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One last item to consider…
NPSH (net positive suction head)
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NPSHR
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NPSHA
NPSH Available 
2.31 Psurface  Pvapor 
sp.gr .
 static head, ft  friction losses, ft
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Biosystems and Ag. Engineering
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NPSHA
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Capacity, Power, Efficiency
• Capacity Q, gpm = 449 x A, ft2 x V, ft/sec
Where A = cross-sectional area of the pipe in ft2
V = velocity of flow in feet per second
• Bhp = actual power delivered to pump shaft
Q  TDH  Sp.Gr .
by driver
bhp

required
3960  pumpefficiency
• Whp = pump output or hydraulic
Q  TDH  Sp.Gr .
horsepower
whp 
3960
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Biosystems and Ag. Engineering
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Pump Efficiency
Ratio of whp to bhp:
whp Q  TDH  Sp.Gr .
PumpEfficiency 

bhp
3960  bhp
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Biosystems and Ag. Engineering
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System Example: 80 ft of 4” ID galv. iron pipe with 3 elbows,
75’ lift, pumps from an open tank, discharges through a pipe to
a tank at atm. Pressure (find rate, imp. dia., eff., motor size,
rpm)
Ratio of whp to bhp:
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Homework Handout
http://biosystems.okstate.edu/Home/jcarol/Class_Notes/
BAE2023_Spring2011/pump hw.pdf
Questions???
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Biosystems and Ag. Engineering
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