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Hydraulic Pumps
>>Performance and Characteristics
General Issues
 Pumps are not strictly continuous
flow devices. Discrete chambers are
involved.
 Flow is collected for discharge
through valve plates
 Design of the valve plate and the
pump mechanism affects pressure
pulses and variation (ripple) of torque
and pressure
General Issues
 Our theoretical displacements can be used
to determine theoretical pump flow
 Qth =Displacement (cc/rev) * Speed (rpm)
 Actual flow is a linear function of pump
displacement, speed, a units constant, and
an efficiency term
 Two kinds of inefficiencies to account for
losses:
 Volumetric efficiency (slip)
 Mechanical efficiency (Friction losses)
Volumetric efficiency
This indicates the amount of leakage, which takes place
within the pump and involves considerations such as
manufacturing tolerances and flexing of the pump
casing.
Actual Pump Output, Q
 QA = (VD np ηV) /1000 where:
Q: L/min
VD : cm3
/rev
ηV: Volumetric efficiency (decimal)
 OR… QA = (VD np ηV) /231 where:
Q: GPM
VD: in3
/rev
ηV: same as above (no units)
Mechanical efficiency
 This indicates the amount of energy lost by
friction in bearing and other moving parts and Energy losses
due to fluid turbulence.
 mech eff =
Mechanical efficiency
 Mechanical efficiency can also be
computed in terms of torque, and
called torque efficency:
overall efficiency
The ratio of power output to power input to the pump
Or the Product of both volumetric and mechanical
efficiencies is known as the overall efficiency
Torque to Drive a Pump
 TA = (ΔP VD)/(2π ηm)
where:
TA : Newton meters torque required
ΔP : pressure rise across the pump in MPa
VD : Pump displacement in cm3
/rev
ηm: Pump mechanical (torque) efficiency – a decimal
 OR…
Torque to Drive a Pump
English Units
 TA = (ΔP VD)/(2π ηm)
where:
TA : is torque required
ΔP : pressure rise across the pump in PSI
VD : Pump displacement in inches3
/rev
ηm: Pump torque efficiency – a decimal
Power to Drive the Pump
 The hydraulic (theoretical) power
delivered by the pump is
QActualΔP/600 or QactualΔP/1714
for SI English units
(note this is actual pump flow, not theoretical)
 Shaft power to drive the pump is
given by Psp = Phydr / ηo where:
 η o = ηv ηm which is total pump efficiency
What Determines ηv & ηm ?
 ηv is a function of clearance spaces, system
pressure, viscosity and pump speed
 Leakage flow at a given pressure is relatively
fixed regardless of pump speed
 It is also affected by fluid viscosity as lower
viscosity fluid will result in higher leakage and
lower volumetric efficiency
What about Torque (mechanical)
Efficiency?
 Torque efficiency is a function of
speed and fluid viscosity
 Higher pump speeds will result in
lower efficiency as viscous friction is
speed dependent
 Lower viscosity fluid can reduce
viscous losses but acts negatively on
volumetric efficiency
Typical Performance curves for pumps
Other Factors affecting pump
performance
• Presence of foreign particles
cause damage to the internal surfaces of a pump.
• Foams and bubbles
Generate noise and causes cavitation
• Overheating of oil
poor lubricant and increases the internal leakage,
reducing pump capacity
• Wrong selection of oil.
select the oil in accordance with the ambient
temperature and follow the instructions of pump
manufacturer
Comparative analysis of
pumps
Cavitation
 Pump cavitation can occur due to entrained air
bubbles in the hydraulic fluid or vaporization of
the hydraulic fluid
 To control cavitation keep the suction pressure
above saturation pressure of fluid by:
 Keeping suction line velocities below 4 ft/sec
(~1m/s) and pump inlet lines as short as possible
 Minimize inlet line fittings; mount pump close to
reservoir; use low-pressure drop filters on inlet, and
use proper oil
Catalogue example
Double pumps
Sizing Pumps
 Component sizing begins with the LOAD
 Load and actuator will determine
 Flow requirement for this circuit
 Pressure range required by the circuit
(We’ll do this with cylinders and motors… soon)
 Total and simultaneous flow requirements
 Select for the maximum load pressure
 Add pressure drops that will occur in valves,
lines and fittings
Pump Sizing
 With pump outlet pressure and flow known
we will consider speed.
 Industrial apps will use synchonous speed of
electric motors. Generally 1750 rpm, or possibly
1100. ($ decides)
 Small diesel apps such as skid loaders can
operate directly from engine crankshaft and will
have engine speed. (2000-3000 rpm).
 Larger diesel apps – pump splitter with gear
reductions possible to optimize speed
Pump Sizing
 Determine appropriate speed for your app
 Use the equation for pump flow, solved for
displacement
 VD = 1000Q/p (np ηV)
 What shall we use for ηV ??
 This is a function of speed, pressure, and
fluid viscosity
 Look for vendor data or curves and adjust…
Pumps Selection
• Flow rate requirement
• Operating speed
• Pressure rating
• Performance
• Reliability
• Maintenance
• Cost and
• Noise.
Pump Symbols
 Any fixed displacement
pump
 Variable displacement
pump
 Variable displacement –
Pressure Compensated

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Hydraulic Pump Performance Characteristics

  • 2. General Issues  Pumps are not strictly continuous flow devices. Discrete chambers are involved.  Flow is collected for discharge through valve plates  Design of the valve plate and the pump mechanism affects pressure pulses and variation (ripple) of torque and pressure
  • 3. General Issues  Our theoretical displacements can be used to determine theoretical pump flow  Qth =Displacement (cc/rev) * Speed (rpm)  Actual flow is a linear function of pump displacement, speed, a units constant, and an efficiency term  Two kinds of inefficiencies to account for losses:  Volumetric efficiency (slip)  Mechanical efficiency (Friction losses)
  • 4. Volumetric efficiency This indicates the amount of leakage, which takes place within the pump and involves considerations such as manufacturing tolerances and flexing of the pump casing.
  • 5. Actual Pump Output, Q  QA = (VD np ηV) /1000 where: Q: L/min VD : cm3 /rev ηV: Volumetric efficiency (decimal)  OR… QA = (VD np ηV) /231 where: Q: GPM VD: in3 /rev ηV: same as above (no units)
  • 6. Mechanical efficiency  This indicates the amount of energy lost by friction in bearing and other moving parts and Energy losses due to fluid turbulence.  mech eff =
  • 7. Mechanical efficiency  Mechanical efficiency can also be computed in terms of torque, and called torque efficency:
  • 8. overall efficiency The ratio of power output to power input to the pump Or the Product of both volumetric and mechanical efficiencies is known as the overall efficiency
  • 9. Torque to Drive a Pump  TA = (ΔP VD)/(2π ηm) where: TA : Newton meters torque required ΔP : pressure rise across the pump in MPa VD : Pump displacement in cm3 /rev ηm: Pump mechanical (torque) efficiency – a decimal  OR…
  • 10. Torque to Drive a Pump English Units  TA = (ΔP VD)/(2π ηm) where: TA : is torque required ΔP : pressure rise across the pump in PSI VD : Pump displacement in inches3 /rev ηm: Pump torque efficiency – a decimal
  • 11. Power to Drive the Pump  The hydraulic (theoretical) power delivered by the pump is QActualΔP/600 or QactualΔP/1714 for SI English units (note this is actual pump flow, not theoretical)  Shaft power to drive the pump is given by Psp = Phydr / ηo where:  η o = ηv ηm which is total pump efficiency
  • 12. What Determines ηv & ηm ?  ηv is a function of clearance spaces, system pressure, viscosity and pump speed  Leakage flow at a given pressure is relatively fixed regardless of pump speed  It is also affected by fluid viscosity as lower viscosity fluid will result in higher leakage and lower volumetric efficiency
  • 13. What about Torque (mechanical) Efficiency?  Torque efficiency is a function of speed and fluid viscosity  Higher pump speeds will result in lower efficiency as viscous friction is speed dependent  Lower viscosity fluid can reduce viscous losses but acts negatively on volumetric efficiency
  • 15. Other Factors affecting pump performance • Presence of foreign particles cause damage to the internal surfaces of a pump. • Foams and bubbles Generate noise and causes cavitation • Overheating of oil poor lubricant and increases the internal leakage, reducing pump capacity • Wrong selection of oil. select the oil in accordance with the ambient temperature and follow the instructions of pump manufacturer
  • 17. Cavitation  Pump cavitation can occur due to entrained air bubbles in the hydraulic fluid or vaporization of the hydraulic fluid  To control cavitation keep the suction pressure above saturation pressure of fluid by:  Keeping suction line velocities below 4 ft/sec (~1m/s) and pump inlet lines as short as possible  Minimize inlet line fittings; mount pump close to reservoir; use low-pressure drop filters on inlet, and use proper oil
  • 20. Sizing Pumps  Component sizing begins with the LOAD  Load and actuator will determine  Flow requirement for this circuit  Pressure range required by the circuit (We’ll do this with cylinders and motors… soon)  Total and simultaneous flow requirements  Select for the maximum load pressure  Add pressure drops that will occur in valves, lines and fittings
  • 21. Pump Sizing  With pump outlet pressure and flow known we will consider speed.  Industrial apps will use synchonous speed of electric motors. Generally 1750 rpm, or possibly 1100. ($ decides)  Small diesel apps such as skid loaders can operate directly from engine crankshaft and will have engine speed. (2000-3000 rpm).  Larger diesel apps – pump splitter with gear reductions possible to optimize speed
  • 22. Pump Sizing  Determine appropriate speed for your app  Use the equation for pump flow, solved for displacement  VD = 1000Q/p (np ηV)  What shall we use for ηV ??  This is a function of speed, pressure, and fluid viscosity  Look for vendor data or curves and adjust…
  • 23. Pumps Selection • Flow rate requirement • Operating speed • Pressure rating • Performance • Reliability • Maintenance • Cost and • Noise.
  • 24. Pump Symbols  Any fixed displacement pump  Variable displacement pump  Variable displacement – Pressure Compensated