Isothermal Liquid Predefined Properties (IL)
Sets the properties of the working fluid for the isothermal fluid network.
blockType: EngeeFluids.IsothermalLiquid.Utilities.PredefinedProperties
Path in the library:
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Description
Block Isothermal Liquid Predefined Properties (IL) sets the properties of the working fluid for the isothermal fluid network in accordance with the properties of the predefined fluid.
The air dissolved in the system can be modeled as a function of pressure. To set your own properties of the working fluid, use the block Isothermal Liquid Properties (IL). If you do not specify a liquid, the default values will be used in the system.
Range of liquid properties
You can configure the block to simulate the properties of several different predefined liquids using the parameter Isothermal liquid.
Voda
The unit provides water properties in the range between the triple point, when the temperature and pressure of the liquid reach 273.160 To and 611.657 Pa, and the critical point when the temperature of the liquid reaches 647.096 K. Value It is set by the pressure at the triple point or the saturation pressure, whichever is greater.
Mixtures of ethylene, propylene and glycerin with water_
The block provides properties for ethylene glycol, propylene glycol, and glycerol at temperatures above the freezing point of the solution.
When setting the mixture, you can determine the concentration of ethylene glycol, propylene glycol, or glycerol in water by mass or volume fraction using the parameter Concentration type.
The block provides properties for:
-
ethylene glycol with a mass fraction of
0before0.6and the volume fraction of0before1; -
propylene glycol with a mass fraction of
0before0.6and the volume fraction of0.1before0.6; -
glycerin with a mass fraction of
0before0.6. You cannot model the volume fraction of glycerol.
The block stores properties as a function of temperature and concentration. The unit retains all properties except for density and coefficient of thermal expansion. , as constants for the pressure range.
_ Sea water_
The block provides properties for seawater for temperatures from 273.15 To before 393.15 K and pressures above the saturation pressure in the system. The salt concentration may vary from 0 before 0.12 by weight.
The block stores properties in tabular form depending on pressure and temperature.
The data for the block is obtained from the software on the website https://web.mit.edu/seawater/.
Jet-A Aviation Fuel_
The unit provides properties for a common, representative fuel mixture based on Jet-A-4658 and Jet-A-3638 substitutes at temperatures from 222.22 To before 645.61 K and pressures above the saturation point.
The unit stores the characteristics in tabular form depending on pressure and temperature.
diesel fuel
The block provides properties for diesel fuel at temperatures from 238.20 To before 690.97 K and pressures above the saturation point.
SAE 5W-30
The block provides properties for SAE 5W-30 at temperatures from 235.15 To before 473.15 To and pressures above 0.01 MPa. The block determines the properties based on the values of the system temperature and atmospheric pressure for temperatures from 29.85 °C to 74.85 °C (from 303 K before 348 K) and pressures from 7 MPa up to 87 MPa. The block uses curve approximation to determine properties in extrapolated regions.
_ Lubricating oils and hydraulic fluids_
The block uses numerical approximations to calculate the properties of the following liquids:
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SAE 30 Oil; -
SAE 50 Oil; -
10W Oil; -
30W Oil; -
50W Oil; -
Skydrol LD-4; -
Skydrol 500B-4; -
Skydrol 5; -
HyJet-IVA; -
Fluid MIL-F-83282; -
Fluid MIL-F-5606; -
Fluid MIL-F-87257; -
ATF (DEXRON III); -
ISO VG 22 (Mobil UNIVIS N 22); -
ISO VG 32 (Mobil UNIVIS N 32); -
ISO VG 46 (Mobil UNIVIS N 46); -
ISO VG 68; -
Brake fluid DOT 3; -
Brake fluid DOT 4; -
Brake fluid DOT 5.
The block uses the Walter equation to approximate velocity changes. depending on the temperature :
where , and — constants specific to each liquid.
The block assumes that the density of it varies linearly depending on the temperature:
where
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— a constant specific to each liquid;
-
— the density of the liquid at the reference temperature .
Volumetric modulus of elasticity defined as
where — the speed of sound. The block uses the value for the speed of sound in hydraulic oils 1460 m/s.
benzine
The unit uses the same approximations as for lubricating oils and hydraulic fluids to calculate the density and volumetric modulus of elasticity of gasoline. In gasoline, the speed of sound is 1250 m/s.
The viscosity of gasoline is calculated using the Vogel—Fulcher—Tamman equation.:
where , and — constants.
Dissolved air
In the block, you can simulate the dissolution of air in a liquid system. If you check the box Model air dissolution, then the block simulates dissolution in the pressure range, which is determined by the values of the parameters Atmospheric pressure and Pressure at which all entrained air is dissolved using Henry’s law.
Ports
Conserving
#
A
—
connection port
Isothermal liquid
Details
Isothermal liquid port connecting the unit to the network. It can be connected to any point of the isothermal liquid connection line on the block diagram. When connecting the block Isothermal Liquid Predefined Properties (IL) to the connecting line, the properties of the liquid extend to all blocks in the circuit.
| Program usage name |
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Parameters
Liquid
#
Isothermal liquid —
liquid selection
Water | Seawater (MIT model) | Ethylene glycol and water mixture | Propylene glycol and water mixture | Glycerol and water mixture | Aviation fuel Jet-A | Diesel fuel | SAE 5W-30 | SAE 30 Oil | SAE 50 Oil | 10W Oil | 30W Oil | 50W Oil | Skydrol LD-4 | Skydrol 500B-4 | Skydrol 5 | HyJet-IVA | Fluid MIL-F-83282 | Fluid MIL-F-5606 | Fluid MIL-F-87257 | ATF (DEXRON III) | ISO VG 22 (Mobil UNIVIS N 22) | ISO VG 32 (Mobil UNIVIS N 32) | ISO VG 46 (Mobil UNIVIS N 46) | ISO VG 68 | Brake fluid DOT 3 | Brake fluid DOT 4 | Brake fluid DOT 5 | Gasoline
Details
Selection of the working fluid in the system.
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For these liquids, the unit calculates the properties of the liquid by interpolating experimental data.:
For other liquids, the block uses approximations to calculate the properties of the liquid. For these approximate liquids, the unit may produce unexpected results at extreme temperatures or if the liquid deviates significantly from atmospheric pressure. |
| Values |
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| Default value |
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| Program usage name |
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| Evaluatable |
No |
#
System temperature —
network temperature
K | degC | degF | degR | deltaK | deltadegC | deltadegF | deltadegR
Details
The temperature in the isothermal fluid network.
| Units |
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| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
# Viscosity derating factor — correction factor for viscosity
Details
Correction factor for liquids whose viscosity deviates from the standard viscosity of a pure liquid.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
#
Atmospheric pressure —
ambient pressure
Pa | uPa | hPa | kPa | MPa | GPa | kgf/m^2 | kgf/cm^2 | kgf/mm^2 | mbar | bar | kbar | atm | ksi | psi | mmHg | inHg
Details
Ambient pressure.
| Units |
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| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
#
Pressure below minimum valid value —
notification when pressure values exceed the minimum allowable value
None | Error
Details
Choose what happens if the liquid pressure exceeds the minimum allowable value during the simulation.:
-
None— the unit does not return an error if the pressure exceeds the minimum allowable value.; -
Error— the block returns an error and stops the simulation.
| Values |
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| Default value |
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| Program usage name |
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| Evaluatable |
No |
# Dissolved salt mass fraction (salinity) — salt concentration
Details
The mass fraction of salt in water, set as a dimensionless value in the range (0, 0.12].
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Seawater (MIT model).
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
#
Concentration type —
concentration by mass or volume
Volume fraction | Mass fraction
Details
It is indicated how the concentration of ethylene glycol or propylene glycol dissolved in water is measured: by weight or by volume.
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Propylene glycol and water mixture or Ethylene glycol and water mixture.
| Values |
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| Default value |
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| Program usage names |
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| Evaluatable |
No |
# Ethylene glycol volume fraction — volume fraction of ethylene glycol
Details
The volume fraction of ethylene glycol in water, set as a dimensionless value in the range (0, 1.0].
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Ethylene glycol and water mixture, and for the parameter Concentration type meaning Volume fraction.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
#
Isothermal bulk modulus at atmospheric pressure (no entrained air) —
volumetric modulus of elasticity
Pa | uPa | hPa | kPa | MPa | GPa | kgf/m^2 | kgf/cm^2 | kgf/mm^2 | mbar | bar | kbar | atm | ksi | psi | mmHg | inHg
Details
The volumetric modulus of elasticity of a solution of ethylene glycol, propylene glycol, or glycerol at atmospheric pressure.
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Ethylene glycol and water mixture, Propylene glycol and water mixture or Glycerol and water mixture.
| Units |
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| Default value |
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| Program usage names |
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| Evaluatable |
Yes |
#
Minimum valid pressure —
the lowest allowable pressure of an ethylene glycol, propylene glycol, or glycerin solution
Pa | uPa | hPa | kPa | MPa | GPa | kgf/m^2 | kgf/cm^2 | kgf/mm^2 | mbar | bar | kbar | atm | ksi | psi | mmHg | inHg
Details
The lowest allowable pressure of an ethylene glycol, propylene glycol, or glycerin solution during simulation. Parameter value Atmospheric pressure must be greater than or equal to Minimum valid pressure.
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Ethylene glycol and water mixture, Propylene glycol and water mixture or Glycerol and water mixture.
| Units |
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| Default value |
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| Program usage names |
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| Evaluatable |
Yes |
# Ethylene glycol mass fraction — mass fraction of ethylene glycol
Details
The mass fraction of ethylene glycol in water, set as a dimensionless value in the range (0, 0.6].
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Ethylene glycol and water mixture, and for the parameter Concentration type meaning Mass fraction.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
# Propylene glycol volume fraction — volume fraction of propylene glycol
Details
The volume fraction of propylene glycol in water, set as a dimensionless value in the range [0.1, 0.6].
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Propylene glycol and water mixture, and for the parameter Concentration type meaning Volume fraction.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
# Propylene glycol mass fraction — mass fraction of propylene glycol
Details
The mass fraction of propylene glycol in water, given as a dimensionless value in the range (0, 0.6].
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Propylene glycol and water mixture, and for the parameter Concentration type meaning Mass fraction.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
# Glycerol mass fraction — mass fraction of glycerol
Details
The mass fraction of glycerol in water, set as a dimensionless value in the range (0, 0.6].
Dependencies
To use this parameter, set for the parameter Isothermal liquid meaning Glycerol and water mixture, and for the parameter Concentration type meaning Mass fraction.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
Entrained Air
# Volumetric fraction of entrained air in mixture at atmospheric pressure — volume fraction of entrained air in a liquid mixture
Details
The volume fraction of air entrained in a mixture of liquids at atmospheric pressure.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
# Air polytropic index — air polytropy indicator
Details
An exponent in an equation describing a polytropic process that relates pressure and volume of a liquid.
| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
#
Air density at atmospheric condition —
air density under atmospheric conditions
kg/m^3 | g/m^3 | g/cm^3 | g/mm^3 | lbm/ft^3 | lbm/gal | lbm/in^3
Details
Air density at pressure Atmospheric pressure.
| Units |
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| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
# Model air dissolution — The dissolution of air
Details
Choose an air dissolution model for an isothermal liquid.
-
If the flag is unchecked, the amount of entrained air remains constant. The dissolution of air is not simulated.
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If this option is selected, the entrained air may dissolve into the liquid. The dissolution of air in a liquid is modeled in the pressure range, which is determined by the values of the parameters Atmospheric pressure and Pressure at which all entrained air is dissolved, according to Henry’s law.
| Default value |
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| Program usage name |
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| Evaluatable |
No |
#
Pressure at which all entrained air is dissolved —
the pressure at which all entrained air is dissolved
Pa | uPa | hPa | kPa | MPa | GPa | kgf/m^2 | kgf/cm^2 | kgf/mm^2 | mbar | bar | kbar | atm | ksi | psi | mmHg | inHg
Details
The pressure at which all the air is dissolved in a liquid.
Dependencies
To use this option, check the box Model air dissolution.
| Units |
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| Default value |
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| Program usage name |
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| Evaluatable |
Yes |
Literature
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Massachusetts Institute of Technology (MIT). Thermophysical properties of seawater database. http://web.mit.edu/seawater.
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K.G. Nayar, M.H. Sharqawy, L.D. Banchik, J.H. Lienhard V. Thermophysical properties of seawater: A review and new correlations that include pressure dependence. Desalination 390 (July 2016): 1–24.
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M.H. Sharqawy, J.H. Lienhard V, S.M. Zubair. Thermophysical properties of seawater: A review of existing correlations and data. Desalination and Water Treatment 16, no. 1–3 (april 2010): 354–380.
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I.H. Bell, J. Wronski, S. Quoilin, V. Lemort. Pure and Pseudo-pure Fluid Thermophysical Property Evaluation and the Open-Source Thermophysical Property Library CoolProp. Industrial & Engineering Chemistry Research 53, no. 6 (February 12, 2014): 2498–2508.