Tank with three hydraulic ports, constant pressurization, and volume-dependent fluid level
Low-Pressure Blocks
The Variable Head Three-Arm Tank block represents a three-arm pressurized tank, in which fluid is stored under a specified pressure. The pressurization remains constant regardless of volume change. The block accounts for the fluid level change caused by the volume variation, as well as for pressure loss in the connecting pipes that can be caused by a filter, fittings, or some other local resistance. The loss is specified with the pressure loss coefficients. The block computes the volume of fluid in the tank and exports it outside through the physical signal port V.
For reasons of computational robustness, the pressure loss in each of the connecting pipes is computed with the equations similar to that used in the Fixed Orifice block:
$${q}_{A}=\sqrt{\frac{1}{{K}_{A}}}\cdot {A}_{A}\sqrt{\frac{2}{\rho}}\cdot \frac{{p}_{lossA}}{{\left({p}_{lossA}^{2}+{p}_{crA}^{2}\right)}^{1/4}}$$
$${q}_{B}=\sqrt{\frac{1}{{K}_{B}}}\cdot {A}_{B}\sqrt{\frac{2}{\rho}}\cdot \frac{{p}_{lossB}}{{\left({p}_{lossB}^{2}+{p}_{crB}^{2}\right)}^{1/4}}$$
$${q}_{C}=\sqrt{\frac{1}{{K}_{C}}}\cdot {A}_{C}\sqrt{\frac{2}{\rho}}\cdot \frac{{p}_{lossC}}{{\left({p}_{lossC}^{2}+{p}_{crC}^{2}\right)}^{1/4}}$$
$${p}_{crA}={K}_{A}\frac{\rho}{2}{\left(\frac{{\mathrm{Re}}_{cr}\cdot \nu}{{d}_{A}}\right)}^{2}$$
$${p}_{crB}={K}_{B}\frac{\rho}{2}{\left(\frac{{\mathrm{Re}}_{cr}\cdot \nu}{{d}_{B}}\right)}^{2}$$
$${p}_{crC}={K}_{C}\frac{\rho}{2}{\left(\frac{{\mathrm{Re}}_{cr}\cdot \nu}{{d}_{C}}\right)}^{2}$$
The Critical Reynolds number is set to 15.
The pressure at the tank outlets is computed with the following equations:
$${p}_{A}={p}_{elev}{}_{A}-{p}_{loss}{}_{A}+{p}_{pr}$$
$${p}_{B}={p}_{elev}{}_{B}-{p}_{loss}{}_{B}+{p}_{pr}$$
$${p}_{C}={p}_{elev}{}_{C}-{p}_{loss}{}_{C}+{p}_{pr}$$
$${p}_{elevA}=\rho \xb7g\xb7H$$
$${p}_{elevB}=\rho \xb7g(H-{h}_{BA})$$
$${p}_{elevC}=\rho \xb7g(H-{h}_{CA})$$
$${A}_{A}=\frac{\pi \xb7{d}_{A}{}^{2}}{4}$$
$${A}_{B}=\frac{\pi \xb7{d}_{B}{}^{2}}{4}$$
$${A}_{C}=\frac{\pi \xb7{d}_{C}{}^{2}}{4}$$
$$H=\{\begin{array}{ll}\frac{V}{A}\hfill & \text{forconstant-areatank}\hfill \\ f(V)\hfill & \text{fortable-specifiedtank}\hfill \end{array}$$
$$V={V}_{0}+q\xb7t$$
where
p_{A} | Pressure at the tank outlet A |
p_{B} | Pressure at the tank outlet B |
p_{C} | Pressure at the tank outlet C |
p_{elevA} | Pressure due to fluid level at outlet A |
p_{elevB} | Pressure due to fluid level at outlet B |
p_{elevC} | Pressure due to fluid level at outlet C |
p_{lossA} | Pressure loss in the connecting pipe A |
p_{lossB} | Pressure loss in the connecting pipe B |
p_{lossC} | Pressure loss in the connecting pipe C |
p_{pr} | Pressurization |
ρ | Fluid density |
g | Acceleration of gravity |
H | Fluid level with respect to outlet A |
h_{AB} | Elevation of outlet B with respect to outlet A |
h_{AC} | Elevation of outlet C with respect to outlet A |
K_{A} | Pressure loss coefficient at outlet A |
K_{B} | Pressure loss coefficient at outlet B |
K_{C} | Pressure loss coefficient at outlet C |
A_{A} | Connecting pipe area at outlet A |
A_{B} | Connecting pipe area at outlet B |
A_{C} | Connecting pipe area at outlet C |
d_{A} | Connecting pipe diameter at outlet A |
d_{B} | Connecting pipe diameter at outlet B |
d_{C} | Connecting pipe diameter at outlet C |
q_{A} | Flow rate through outlet A |
q_{B} | Flow rate through outlet B |
q_{C} | Flow rate through outlet C |
p_{crA} | Minimum pressure for turbulent flow in the connecting pipe A |
p_{crB} | Minimum pressure for turbulent flow in the connecting pipe B |
p_{crC} | Minimum pressure for turbulent flow in the connecting pipe C |
V | Instantaneous fluid volume |
V_{0} | Initial fluid volume |
A | Tank cross-sectional area |
t | Simulation time |
For a tank with a variable cross-sectional area, the relationship between fluid level and volume is specified with the table lookup
$$H=f(V)$$
You have a choice of two interpolation methods and two extrapolation methods.
Connections A, B, and C are hydraulic conserving ports associated with the tank outlets. Connection V is a physical signal port. The flow rates are considered positive if fluid flows into the tank.
Warning If fluid level becomes so low that some of the tank outlets get exposed, no warnings will be issued. The simulation will continue and pressure at exposed outlet(s) will be set to the pressurization pressure level. If this is not acceptable, MathWorks recommends that you employ the necessary control measures to guard against this situation in your models. |
The initial volume of fluid in the tank. This parameter must
be greater than zero. The default value is 20
l.
Gage pressure acting on the surface of the fluid in the tank. It can be created by a gas cushion, membrane, bladder, or piston, as in bootstrap reservoirs. This parameter must be greater than or equal to zero. The default value is 0, which corresponds to a tank connected to atmosphere.
Select one of the following block parameterization options:
Linear
— Provide
a value for the tank cross-sectional area. The level is assumed to
be linearly dependent on the fluid volume. This is the default method.
Table-specified
—
Provide tabulated data of fluid volumes and fluid levels. The level
is determined by one-dimensional table lookup. You have a choice of
two interpolation methods and two extrapolation methods.
The cross-sectional area of the tank. This parameter must be
greater than zero. The default value is 0.8
m^2.
This parameter is used if Level/Volume relationship is
set to Linear
.
Specify the vector of input values for fluid volume as a one-dimensional
array. The input values vector must be strictly increasing. The values
can be nonuniformly spaced. The minimum number of values depends on
the interpolation method: you must provide at least two values for
linear interpolation, at least three values for smooth interpolation.
The default values, in m^3, are [0 0.0028 0.0065 0.0114 0.0176
0.0252 0.0344 0.0436 0.0512 0.0574 0.0623 0.066 0.0688 0.0707 0.072
0.0727]
. This parameter is used if Level/Volume
relationship is set to Table-specified
.
Specify the vector of fluid levels as a one-dimensional array.
The fluid levels vector must be of the same size as the fluid volumes
vector. The default values, in meters, are [0 0.02 0.04 0.06
0.08 0.1 0.12 0.14 0.16 0.18 0.2 0.22 0.24 0.26 0.28 0.3]
.
This parameter is used if Level/Volume relationship is
set to Table-specified
.
The diameter of the connecting pipe at port A. This parameter
must be greater than zero. The default value is 0.025
m.
The value of the pressure loss coefficient, to account for pressure
loss in the connecting pipe at port A. This parameter must be greater
than zero. The default value is 1.2
.
The diameter of the connecting pipe at port B. This parameter
must be greater than zero. The default value is 0.02
m.
The elevation of port B above port A. If port A is higher than
port B, enter a negative value. The default value is 0.8
m.
The value of the pressure loss coefficient, to account for pressure
loss in the connecting pipe at port B. The loss is computed with the
equation similar to the one given for port A. This parameter must
be greater than zero. The default value is 1.2
.
The diameter of the connecting pipe at port C. This parameter
must be greater than zero. The default value is 0.02
m.
The elevation of port C above port A. If port A is higher than
port C, enter a negative value. The default value is 0.8
m.
The value of the pressure loss coefficient, to account for pressure
loss in the connecting pipe at port C. The loss is computed with the
equation similar to the one given for port A. This parameter must
be greater than zero. The default value is 1.2
.
Select one of the following interpolation methods for approximating the output value when the input value is between two consecutive grid points:
Linear
— Select
this option to get the best performance.
Smooth
— Select
this option to produce a continuous curve with continuous first-order
derivatives.
For more information on interpolation algorithms, see the PS Lookup Table (1D) block reference page.
This parameter is used if Level/Volume relationship is
set to Table-specified
.
Select one of the following extrapolation methods for determining the output value when the input value is outside the range specified in the argument list:
Linear
— Select
this option to produce a curve with continuous first-order derivatives
in the extrapolation region and at the boundary with the interpolation
region.
Nearest
— Select
this option to produce an extrapolation that does not go above the
highest point in the data or below the lowest point in the data.
For more information on extrapolation algorithms, see the PS Lookup Table (1D) block reference page.
This parameter is used if Level/Volume relationship is
set to Table-specified
.
The block has the following ports:
A
Hydraulic conserving port associated with the tank outlet A.
B
Hydraulic conserving port associated with the tank outlet B.
C
Hydraulic conserving port associated with the tank outlet C.
V
Physical signal port that outputs the volume of fluid in the tank.