Pressure Reducing Valve (TL)
Pressure reducing valve in a thermal liquid network
Libraries:
Simscape /
Fluids /
Thermal Liquid /
Valves & Orifices /
Pressure Control Valves
Description
The Pressure Reducing Valve (TL) block represents a valve that reduces downstream pressure in a thermal liquid network. The valve remains open when the pressure at port B is less than a specified pressure. When the pressure at port B meets or surpasses this pressure, the valve closes. The block operates based on the differential between the set pressure and the pressure at port B. The block contains a check valve portion that functions identically to the Check Valve (TL) block during flow reversals.
Pressure Control
The block regulates pressure between the set pressure and maximum pressure. When you set Set pressure control to:
Controlled
— You can connect a pressure signal to port Ps. The block regulates pressure when the pressure at port B is greater than the reference set pressure, Pset, and below Pmax. The pressure at port B acts as the control pressure, Pcontrol, for this valve.Pmax is the sum of Pset and the pressure regulation range.
Constant
— The Set pressure (gauge) parameter defines a constant set pressure.
The normalized pressure, , controls the valve opening area when Opening
parameterization is Linear - Area vs.
pressure
. The normalized pressure is
where:
pcontrol is the control pressure, pB ̶ pAtm, where pAtm is the atmospheric pressure.
pset is the valve set pressure
where Pset,gauge is the value of the Set pressure (gauge) parameter.
pmax is the maximum pressure, pmax = pset + prange, where prange is the value of the Pressure regulation range parameter.
Opening Parameterization
The mass flow rate depends on the value of the Opening parameterization parameter.
When you set Opening parameterization to
Linear - Area vs. pressure
or
Tabulated data - Area vs. pressure
, the mass flow
rate is
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.
is the average fluid density.
Δp is the valve pressure difference pA – pB.
The critical pressure difference, Δpcrit, is the pressure differential associated with the Critical Reynolds number, Recrit, the flow regime transition point between laminar and turbulent flow:
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 PRloss as
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.
When you set the Opening parameterization parameter to
Linear - Area vs. pressure
, the block calculates
the opening area as
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 using the linear parameterization.
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 data - Area vs. pressure
, the block
calculates the opening area as
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 shows how the block controls the opening area when
Opening parameterization is Tabulated data
- Area vs. pressure
.
When you set Opening parameterization to
Tabulated data - Volumetric flow rate vs.
pressure
, the valve opens according to the user-provided
tabulated data of volumetric flow rate and pressure differential between ports
A and B.
The block calculates the mass flow rate as
where:
is the volumetric flow rate.
is the average fluid density.
The block calculates the relationship between the mass flow and pressure using
where
Opening Dynamics
When you select Opening dynamics, the block introduces a control pressure lag where pcontrol becomes the dynamic control pressure, pdyn. The instantaneous change in dynamic opening area is calculated based on the Opening time constant parameter, τ:
By default, the block clears the Opening dynamics check box.
Energy Balance
The energy conservation equation in the valve is
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.
Three fault options are available for the reducing valve and check valve. For the Reducing valve opening when faulted and Check valve opening when faulted parameters, you can choose:
Closed
— The valve shuts to its smallest opening value, depending on the Opening parameterization parameter. When you set Opening parameterization to:Linear - Area vs. pressure
— The valve area reduces to the value of the Leakage area parameter.Tabulated data - Area vs. pressure
— The valve area reduces to the value of the last element in the Opening area vector parameter.Tabulated data - Volumetric flow rate vs. pressure
— The flow coefficient reduces to the value of the last element of the derived flow coefficient lookup table, KTLU,Ref.
Open
— The valve opens to its largest opening value, depending on the Opening parameterization parameter. When you set Opening parameterization to:Linear - Area vs. pressure
— The valve area opens to the value of the Maximum opening area.Tabulated data - Area vs. pressure
— The valve area opens to the value of the first element in the Opening area vector.Tabulated data - Volumetric flow rate vs. pressure
— The flow coefficient reduces to the value of the first element of the derived flow coefficient lookup table, KTLU,Ref.
Maintain last value
— The valve area remains at the valve opening area when the trigger occurred.
For the linear parameterization, numerical smoothing at the extremes of the valve area causes the minimum area applied to be larger than the Leakage area parameter, and the maximum is smaller than the Maximum orifice area parameter.
After the fault triggers, the valve remains at the faulted area for the rest of the simulation.
Predefined Parameterization
You can populate the block with pre-parameterized manufacturing data, which allows you to model a specific supplier component.
To load a predefined parameterization:
In the block dialog box, next to Selected part, click the "<click to select>" hyperlink next to Selected part in the block dialogue box settings.
The Block Parameterization Manager window opens. Select a part from the menu and click Apply all. You can narrow the choices using the Manufacturer drop down menu.
You can close the Block Parameterization Manager menu. The block now has the parameterization that you specified.
You can compare current parameter settings with a specific supplier component in the Block Parameterization Manager window by selecting a part and viewing the data in the Compare selected part with block section.
Note
Predefined block parameterizations use available data sources to supply parameter values. The block substitutes engineering judgement and simplifying assumptions for missing data. As a result, expect some deviation between simulated and actual physical behavior. To ensure accuracy, validate the simulated behavior against experimental data and refine your component models as necessary.
To learn more, see List of Pre-Parameterized Components.