Hydraulic Servo and Related Systems ME4803 Motion Control

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Presentation transcript:

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 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). Cetinkunt, Sabri, Mechatronics, John Wiley & Sons, Hoboken, NJ, 2007.

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

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

System Overview Volts-amp Electric or IC prime mover Transmission line & valve Flow-press. Motor or cylinder Rpm-torque or force Rpm-torque Flow-press. Pump Coupling mechanism 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 Rpm-torque or force Load

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

Simple open-loop closed-center circuit

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

Pilot operated valve

Proportional Valve

Various valve schematics

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

Orifice Model

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  p0 ps p1, q1 p2, q2 x

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

Dynamic Equations: the Actuator Change in volume Change in density y Net area Ap q1 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

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

Choices for modeling the hydraulic actuator (simplified actuator) Change of variables: consider q as volumetric flow rate With no compliance or compressibility we get actuator velocity v as q Area A m y q 1/A dy/dt With compliance and/or compressibility combined into a factor k And with moving mass m we get the following block diagram. Steady state (dy/dt)/q is the same. Transient is different. (Show with final value theorem.) k  dt q p A/m dv/dt dy/dt A feedback load pressure may reduce q -

Manufacturer’s Data: BD15 Servovalve on HAL

Manufacturer’s Data: BD15 Servovalve on HAL

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

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

Another valve design with direct feedback

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

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 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)

Darcy’s formula from Bernoulli’s Eq.

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

Orifice Model

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

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

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

Stress Formulas for Cylinders or Conduits

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

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

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