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Hydraulic Servo and Related Systems ME4803 Motion Control

Hydraulic Servo and Related Systems ME4803 Motion Control. Wayne J. Book HUSCO/Ramirez Chair in Fluid Power and Motion Control G.W. Woodruff School of Mechanical Engineering Georgia Institute of Technology. Hydraulics is Especially critical to the Mobile Equipment Industry. References.

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Hydraulic Servo and Related Systems ME4803 Motion Control

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  1. Hydraulic Servo and Related SystemsME4803 Motion Control Wayne J. Book HUSCO/Ramirez Chair in Fluid Power and Motion Control G.W. Woodruff School of Mechanical Engineering Georgia Institute of Technology

  2. Hydraulics is Especially critical to the Mobile Equipment Industry

  3. References • Norvelle, F.D. Fluid Power Control Systems, Prentice Hall, 2000. • Fitch, E.C. and Hong I.T. Hydraulic Component Design and Selection, BarDyne, Stillwater, OK, 2001. • Cundiff, J.S. Fluid Power Circuits and Controls, CRC Press, Boca Raton, FL, 2002. • Merritt, H.E. Hydraulic Control Systems, John Wiley and Sons, New York, 1967. • Fluid Power Design Engineers Handbook, Parker Hannifin Company (various editions).

  4. The Strengths of Fluid Power(Hydraulic, to a lesser extent pneumatic) • High force at moderate speed • High power density at point of action • Fluid removes waste heat • Prime mover is removed from point of action • Conditioned power can be routed in flexible a fashion • Potentially “Stiff” position control • Controllable either electrically or manually • Resulting high bandwidth motion control at high forces • NO SUBSTITUTE FOR MANY HEAVY APPLICATIONS

  5. Difficulties with Fluid Power • Possible leakage • Noise generated by pumps and transmitted by lines • Energy loss due to fluid flows • Expensive in some applications • Susceptibility of working fluid to contamination • Lack of understanding of recently graduated practicing engineers • Multidisciplinary • Cost of laboratories • Displaced in curriculum by more recent technologies

  6. Volts-amp System Overview Electric or IC prime mover Transmission line & valve Flow-press. Motor or cylinder Rpm-torque or force Rpm-torque Flow-press. Pump • The system consists of a series of transformation of power variables • Power is either converted to another useful form or waste heat • Impedance is modified (unit force/unit flow) • Power is controlled • Function is achieved Coupling mechanism Rpm-torque or force Load

  7. Simple open-loop open-center circuit cylinder Actuating solenoid Spring return Pressure relief valve 4-way, 3 position valve filter Fixed displacement pump Fluid tank or reservoir

  8. Simple open-loop closed-center circuit

  9. Closed-loop (hydrostatic) system Motor Check valve Variable displacement reversible pump Drain or auxiliary line

  10. Pilot operated valve

  11. Proportional Valve

  12. Basic Operation of the Servo Valve(single stage) Flow exits Flow enters Torque motor moves spool right Torque motor moves spool left Positive motor rotation Negative motor rotation

  13. Orifice Model

  14. p0 ps p0 x p2, q2 p1, q1 4 Way Proportional Spool Valve Model • Spool assumptions • No leakage, equal actuator areas • Sharp edged, steady flow • Opening area proportional to x • Symmetrical • Return pressure is zero • Zero overlap • Fluid assumptions • Incompressible • Mass density 

  15. p0 ps p0 x p2, q2 p1, q1 Dynamic Equations (cont.)

  16. q1 Change in volume y Net area Ap Change in density Dynamic Equations: the Actuator • If truly incompressible: • Specification of flow without a response in pressure brings a causality problem • For example, if the piston has mass, and flow can change instantaneously, infinite force is required for infinite acceleration • Need to account for change of density and compliance of walls of cylinder and tubes

  17. Compressibility of Fluids and Elasticity of Walls For the pure definition, the volume is fixed. More useful here is an effective bulk modulus that includes expansion of the walls and compression of entrapped gasses Using this to solve for the change in pressure

  18. q dv/dt 1/A q p dv/dt k  dt A /m Choices for modeling the hydraulic actuator With no compliance or compressibility we get actuator velocity v as With compliance and/or compressibility combined into a factor k And with moving mass m

  19. Manufacturer’s Data: BD15 Servovalve on HAL

  20. Manufacturer’s Data: BD15 Servovalve on HAL

  21. Two-stage Servo Valve With flapper centered the flow and pressure is balanced Torque motor rotates flapper, obstructs left nozzle Feedback spring balances torque motor force Pressure increases Spool is driven right Flow gives negative rotation

  22. Details of Force Feedback Design 2 Sharp edged orifices, symmetrical opening Shown line to line; no overlap or underlap

  23. Another valve design with direct feedback

  24. Position Servo Block Diagram Flow gain / motor displacement Position measurement Load torque Net flow / displacement Proportional control May be negligible

  25. Design of some components(with issues pertinent to this class) • The conduit (tubing) is subject to requirements for • flow (pressure drop) • 2 to 4 ft/sec for suction line bulk fluid velocity • 7 to 20 ft/sec for pressure line bulk fluid velocity • pressure (stress) • The piston-cylinder is the most common actuator • Must withstand pressure • Must not buckle

  26. Design Equations for Fluid Power Systems • Flow • Darcy’s formula • Orifice flow models • Stress • Thin-walled tubes (t<0.1D) • Thick-walled tubes (t>0.1D) • Guidelines • Fluid speed • Strengths • Factors of safety (light service: 2.5, general: 3.15, heavy: 4-5 or more)

  27. Darcy’s formula from Bernoulli’s Eq.

  28. Friction factor for smooth pipes(empirical) from e.g. Fitch

  29. Orifice Model

  30. Buckling in the Piston Rod (Fitch) • Rod is constrained by cylinder at two points • Constrained by load at one point • Diameter must resist buckling • Theory of composite “swaged column” applies • Composite column fully extended is A-B-E shown below consisting of 2 segments • A-B segment buckles as if loaded by force F on a column A-B-C • B-E segment buckles as if loaded by F on DBE • Require tangency at B

  31. Cylinder construction (tie-rod design) Resulting loading on cylinder walls

  32. Applicable wall thickness stress formulas(conduits or cylinders) • Thin walled cylinders (open, or where only circumferential hoop stress is significant) (Barlow) • Thick walled cylinders • Brittle materials (based on max normal stress) use Lame’s formula • Ductile (based on max strain theory) • Open end (no axial stress) (Birnie) • Closed end (cylinder bears axial stress) (Clavarino) • Expansion of cylinder based on strain = stress/(Young’s modulus)

  33. Stress formulas

  34. Results of Composite Column Model Equating the slope of the two column segments at B where they join yields: Composite column model matches manufacturer’s recommendations with factor of safety of 4

  35. Pressure Specifications • Nominal pressure = expected operating • Design pressure = Nominal • Proof pressure (for test) = 2x Design • Burst pressure (expect failure) = 4x Design

  36. Pipes versus tubes • Tubes are preferred over pipes since fewer joints mean • Lower resistance • Less leakage • Easier construction

  37. Fittings between tube and other components require multiple seals Flared tube design

  38. New Approaches: Independent Metering

  39. Pump x F Ksb Ksa B A Kbt Kat Tank Check Valve Independent Metering: Introduction Independent Metering Configuration

  40. Pump Pump Pump Pump F F F F Pump x x x x Ksb Ksb Ksb Ksb Ksa Ksa F Ksa Ksa Ksb Ksa B B B B B A A A A Kbt Kbt Kbt Kbt A Kat Kat Kat Kat Kbt Tank Tank Tank Tank Kat Check Valve Tank Check Valve Check Valve Check Valve Powered Retraction Low Side Regeneration Extension Check Valve Low Side Regeneration Retraction Powered Extension Mode High Side Regeneration Extension Advantages of Independent Metering: Metering Modes • Energy saving potential: Regenerative flow. Regeneration flow can be defined as pumping the fluid from one chamber to the other to achieve motion control of the load with using no or minimum flow from the pump.

  41. Traditional Valve Independent Metering Valve Configuration P Q Saved Power Losses on Input Valve Useful Power Losses on Output Valve Power Savings Saved Power

  42. Ps, Qs Ps, Qs Pr, Qr a b a b High Side Regeneration Extension Powered Extension Regenerative Modes versus Powered Modes • HSRE vs PE

  43. Using Powered Extension With High Pump Pressure Using High Side Regeneration Extension Saves Pump Flow P P Q Q Saved Power Used Power Lost Power • HSRE vs PE

  44. Using Powered Extension With High Pump Pressure Using Low Side Regeneration Extension Saves Pump Flow and Pressure P P Q Q Saved Power Used Power Lost Power • LSRE vs PE

  45. Vibration Analysis • Effect of Mode Switching

  46. Vibration Analysis • Telehandler Boom

  47. Continuously Variable Modes (CVMs) • Three-Valve Modulation Modes • Use three valves to provide the fluid flow path instead of two valves • Better force-speed capability and better velocity performance

  48. Ps Cylinder Pump Pump qb Cylinder Ksa Ksa qa Kbt Ksb qb Tank qa Ps Pr Continuously Variable Modes (CVMs) • PHSRE

  49. q2 Kbt Ps Pr Ksa b Cylinder q1 Pump qb a Ksa Cylinder q3 Kat qa Kbt Kbt Tank qout Pr qin Kat Pr Check Valve Tank Ps Pr Continuously Variable Modes (CVMs) • PLSRE

  50. Ps qb Ksb q1 b q3 Kbt a Ps qb Pump Pr Cylinder Kat Cylinder q2 Ksb Kbt Pr qin qa qout Kat Pr Kat Pr Tank Tank Continuously Variable Modes (CVMs) • PLSRR

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