Ball Valve
(To be removed) Valve with a sliding ball control mechanism
The Hydraulics (Isothermal) library will be removed in a future release. Use the Isothermal Liquid library instead. (since R2020a)
For more information on updating your models, see Upgrading Hydraulic Models to Use Isothermal Liquid Blocks.
Libraries:
Simscape /
Fluids /
Hydraulics (Isothermal) /
Valves /
Flow Control Valves
Description
The Ball Valve block models an orifice with a variable opening area
controlled by a sliding ball mechanism. The opening area changes with the relative
position of the ball—the valve lift. A displacement toward
the orifice decreases flow while a displacement away increases flow. The interface
between the orifice and the ball—the valve seat—can
be Sharp-edged
, shown left in the figure, or
Conical
, shown right.
Ball Valve Seat Types
Opening Area
The valve lift is a function of the displacement signal specified through port S. The two can, but generally do not, have the same value. The valve lift differs from the displacement whenever the Ball displacement offset parameter is nonzero:
where:
h is the valve lift.
x0 is the ball displacement offset.
s is the ball displacement (relative to the specified offset).
The valve is fully closed when the valve lift is equal to zero or less. It is fully open when the valve lift reaches or exceeds a (geometry-dependent) value sufficient to completely clear the orifice. A fully closed valve has an opening area equal to the specified Leakage area parameter while a fully open valve has the maximum possible opening area. Adjusting for internal leakage:
where:
AMax is the maximum opening area.
rO is the orifice radius.
ALeak is the internal leakage area between the ports.
At intermediate values of the valve lift, the opening area depends on
the valve seat geometry. If the Valve seat specification
parameter is set to Sharp-Edged
, the opening area as a
function of valve lift is:
where:
A is the opening area at a given valve lift value.
rB is the ball radius.
dOB(h) is the distance from the center of the ball (point O in the figure) to the edge of the orifice (point B). This distance is a function of the valve lift (h).
If the Valve seat specification parameter is set
to Conical
, the opening area becomes:
where θ is the angle between the conical surface and the orifice centerline. The geometrical parameters and variables used in the equations are shown in the figure.
Valve Geometries
Flow Rate
The volumetric flow rate through the valve is a function of the opening area, A(h), and of the pressure differential between the valve ports:
where:
CD is the flow discharge coefficient.
ρ is the hydraulic fluid density.
Δp is the pressure differential between the valve ports, defined as:
where pA is the pressure at port A and pB is the pressure at port B.
pCr is the minimum pressure required for turbulent flow.
The critical pressure pCr is computed from the critical Reynolds number as:
where:
ReCr is the critical Reynolds number.
ν (nu) is the hydraulic fluid dynamic viscosity.
DH is the orifice hydraulic diameter:
in which:
DHMin is the minimum hydraulic diameter, corresponding to the smallest attainable flow area, the leakage flow area.
DHMax is the maximum hydraulic diameter, corresponding to the largest attainable flow area, that of the valve in the fully open position.
l is the wetted length of the valve perimeter—which can, but need not, be that of a circle.
Variables
To set the priority and initial target values for the block variables prior to simulation, use the Initial Targets section in the block dialog box or Property Inspector. For more information, see Set Priority and Initial Target for Block Variables.
Nominal values provide a way to specify the expected magnitude of a variable in a model. Using system scaling based on nominal values increases the simulation robustness. Nominal values can come from different sources, one of which is the Nominal Values section in the block dialog box or Property Inspector. For more information, see Modify Nominal Values for a Block Variable.
Assumptions
Fluid inertia is assumed to be negligible.