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Pressure Compensator Valve (TL)

Pressure compensator valve in thermal liquid network

Since R2023a

Libraries:
Simscape / Fluids / Thermal Liquid / Valves & Orifices / Pressure Control Valves

Description

The Pressure Compensator Valve (TL) block represents a pressure compensator in a thermal liquid network, such as a pressure relief valve or pressure reducing valve. Use this block to maintain the pressure at the valve based on signals from another part of the system.

The pressure differential between ports X and Y is the control pressure, Pcontrol. When this value meets or exceeds the set pressure, the valve area opens or closes depending on the Valve specification parameter. The pressure regulation range begins at the set pressure, Pset.

Pressure Control

The block regulates pressure when Pcontrol exceeds Pset. The block continues to regulate the pressure up to Pmax, the sum of Pset and the pressure regulation range. The block supports two modes of regulation:

  • When you set Set pressure control to Controlled and connect a pressure signal to port Ps, the block keeps the pressure regulation range constant. The valve regulates pressure when Pcontrol is greater than the value of the signal at port Ps and less than Pmax.

  • When you set Set pressure control to Constant, the Set pressure differential parameter defines a constant set pressure.

Conservation of Mass

The block conserves mass such that

m˙A+m˙B=0.

The block calculates the mass flow rate through the valve as

m˙=CdAvalve2ρ¯PRloss(1(AvalveAport)2)Δp[Δp2+Δpcrit2]1/4,

where:

  • Cd is the value of the Discharge coefficient parameter.

  • Avalve is the instantaneous valve open area.

  • Aport is the value of the Cross-sectional area at ports A and B parameter.

  • ρ¯ is the average fluid density.

  • Δp is the valve pressure difference pApB.

The critical pressure difference, Δpcrit, is the pressure differential specified by the Critical Reynolds number parameter, Recrit. This parameter represents the flow regime transition point between laminar and turbulent flow. The block finds the critical pressure difference as

Δpcrit=π8Avalveρ¯(μRecritCd)2,

where μ is the dynamic viscosity of the thermal liquid.

The pressure loss, PRloss, describes the reduction of pressure in the valve due to a decrease in area. The block calculates the pressure loss as:

PRloss=1(AvalveAport)2(1Cd2)CdAvalveAport1(AvalveAport)2(1Cd2)+CdAvalveAport.

The pressure recovery describes the positive pressure change in the valve due to an increase in area. When you clear the Pressure recovery check box, the block sets PRloss to 1.

The block calculates Avalve using the opening parameterization and the valve opening dynamics.

Valve Opening Parameterization

When you set Opening parameterization to Linear, the valve area for normally open valves is

Avalve=p^(AleakAmax)+Amax,

where Aleak is the value of the Leakage Area parameter and Amax is the value of the Maximum opening area parameter. This figure shows how the block controls the opening area for a normally open valve using the linear parameterization.

Pressure differential between ports X and Y with respect to opening area for a normally open valve using the linear parameterization

For normally closed valves, the block uses

Avalve=p^(AmaxAleak)+Aleak.

This figure show how the block controls the opening area for a normally closed valve using the linear parameterization.

Pressure differential between ports X and Y with respect to opening area for a normally closed valve using the linear parameterization

The normalized pressure, p^, is

p^=pcontrolpsetpmaxpset.

When the valve is in a near-open or near-closed position in the linear parameterization, you can maintain numerical robustness in your simulation by adjusting the Smoothing factor parameter. If the Smoothing factor parameter is nonzero, the block smoothly saturates the control pressure between pset and pmax. For more information, see Numerical Smoothing.

When you set Opening parameterization to Tabulated, Aleak and Amax are the first and last parameters of the Opening area vector parameter, respectively. The block calculates the opening area as

Avalve=tablelookup(pcontrol,TLU,ref,ATLU,pcontrol,interpolation=linear,extrapolation=nearest),

where:

  • pcontrol,TLU,ref = pTLU + poffset.

  • pTLU is the Pressure differential vector parameter.

  • poffset is an internal pressure offset that causes the valve to start closing when pcontrol,TLU,ref = pset.

  • ATLU is the Opening area vector parameter.

This figure demonstrates how the block controls the opening area for a normally open valve using the tabulated data parameterization.

Pressure differential between ports X and Y with respect to opening area for a normally open valve using the tabulated parameterization

This figure demonstrates how the block controls the opening area for a normally closed valve using the tabulated data parameterization.

Pressure differential between ports X and Y with respect to opening area for a normally closed valve using the tabulated parameterization

Opening Dynamics

When you select Opening dynamics, the block introduces a control pressure lag where pcontrol becomes the dynamic control pressure, pdyn. The block calculates the instantaneous change in dynamic control pressure based on the Opening time constant parameter, τ:

p˙dyn=pcontrolpdynτ.

By default, the block clears the Opening dynamics check box. When Opening parameterization is Linear, a nonzero value for the Smoothing factor parameter provides additional numerical stability when the orifice is in near-closed or near-open position.

The block calculates the steady-state dynamics according to the Opening parameterization parameter based on the control pressure, pcontrol.

Energy Balance

The energy conservation equation in the valve is

ϕA+ϕB=0,

where:

  • ϕA is the energy flow rate into the valve through port A.

  • ϕB is the energy flow rate into the valve through port B.

Faults

To model a fault, in the Faults section, click the Add fault hyperlink next to the fault that you want to model. Use the fault parameters to specify the fault properties. For more information about fault modeling, see Introduction to Simscape Faults.

You can set the Opening area when faulted parameter to:

  • Closed — The valve area stops at its smallest value, depending on the Opening parameterization parameter setting:

    • Linear — The valve area stops at the value of the Leakage area parameter.

    • Tabulated — The valve area stops at the smallest element of the Opening area vector parameter.

  • Open — The valve stops at its largest value, depending on the Opening parameterization parameter setting:

    • Linear — The valve area stops at the value of the Maximum opening area parameter.

    • Tabulated — The valve area stops at the largest element of the Opening area vector parameter.

  • Maintain last value — The valve area stops at the valve open area when the trigger occurred.

Due to numerical smoothing at the extremes of the valve area, the minimum area the block uses is larger than the leakage area, and the maximum is smaller than the value of the Maximum orifice area parameter. This effect is in proportion to the amount of smoothing you apply.

After the fault triggers, the valve remains at the faulted area for the rest of the simulation.

Ports

Conserving

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Thermal liquid conserving port associated with the A side of the valve.

Thermal liquid conserving port associated with the B side of the valve.

Thermal liquid conserving port associated with the pressure at point X, Px.

Thermal liquid conserving port associated with point Y, Py.

Input

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Pressure differential for controlled valve operation, in Pa.

Dependencies

To enable this port, set Set pressure control to Controlled.

Parameters

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Parameters

Normal operating condition of the pressure compensator valve. For a reducing valve, choose Normally open valve. For a relief valve, choose Normally closed.

Valve operation method. When you set this parameter to:

  • Controlled and connect a pressure signal to port Ps, the block keeps the pressure regulation range constant. The valve regulates pressure when Pcontrol is greater than the value of the signal at port Ps and less than Pmax.

  • Constant, the Set pressure differential parameter defines a constant set pressure.

Method used to parameterize the opening action of the valve.

Magnitude of the pressure differential that triggers pressure compensation.

Dependencies

To enable this parameter, set Set pressure control to Constant.

Operational pressure range of the valve. The pressure regulation range defines the difference between the Set pressure differential parameter and the maximum valve operating pressure.

Dependencies

To enable this parameter, set Opening parameterization to Linear.

Cross-sectional area of the valve in the fully open position.

Dependencies

To enable this parameter, set Opening parameterization to Linear.

Sum of all gaps when the valve is in the fully closed position. An area smaller than this value saturates to the specified leakage area. This value contributes to numerical stability by maintaining continuity in the flow.

Dependencies

To enable this parameter, set Opening parameterization to Linear.

Vector of pressure differential values for the tabulated parameterization of the opening area. The vector elements must correspond one-to-one to the values in the Opening area vector parameter. The pressures must be in ascending order.

Dependencies

To enable this parameter, set Opening parameterization to Tabulated.

Vector of opening area values for the tabulated parameterization of the opening area. The vector elements must correspond one-to-one to the values in the Pressure differential vector parameter. For normally open valves, list elements in descending order. For normally closed valves, list elements in ascending order.

The opening area vector must have the same number of elements as the Pressure differential vector parameter. The block uses linear interpolation between table data points.

Dependencies

To enable this parameter, set Opening parameterization to Tabulated.

Cross-sectional area at the entry and exit ports A and B. The block uses this area in the pressure-flow rate equation that determines mass flow rate through the valve.

Correction factor that the block uses to account for discharge losses in theoretical flows.

Upper Reynolds number limit for laminar flow through the valve.

Continuous smoothing factor that the block uses to introduce a layer of gradual change to the flow response when the valve is in near-open or near-closed positions. Set this parameter to a nonzero value less than one to increase the stability of your simulation in these regimes.

Dependencies

To enable this parameter, set Opening parameterization to Linear.

Whether to account for pressure increase when fluid flows from a region of a smaller cross-sectional area to a region of larger cross-sectional area.

Whether to account for transient effects to the fluid system due to the valve opening. When you select this parameter, the block approximates the opening conditions by introducing a first-order lag in the flow response.

Time constant by which to compute the lag in the opening dynamics.

Dependencies

To enable this parameter, select Opening dynamics.

Faults

Option to model a valve area fault in the block. To add a fault, click the Add fault hyperlink. After a fault, the block sets the valve area based on the value specified in the Opening area when faulted parameter.

Faulted opening area. You can choose for the valve to seize when the valve is opened, closed, or at the area after a fault.

Dependencies

To enable this parameter, enable faults for the block by clicking the Add fault hyperlink.

Extended Capabilities

C/C++ Code Generation
Generate C and C++ code using Simulink® Coder™.

Version History

Introduced in R2023a

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