| 1 | within Modelica; |
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| 2 | package Media "Library of media property models" |
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| 3 | extends Modelica.Icons.Library; |
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| 4 | import SI = Modelica.SIunits; |
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| 5 | |
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| 6 | |
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| 7 | annotation ( |
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| 8 | version="1.0", |
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| 9 | versionDate="2005-03-01", |
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| 10 | preferedView="info", |
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| 11 | Documentation(info="<HTML> |
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| 12 | <p> |
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| 13 | This library contains <a href=\"Modelica://Modelica.Media.Interfaces\">interface</a> |
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| 14 | definitions for media and the following <b>property</b> models for |
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| 15 | single and multiple substance fluids with one and multiple phases: |
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| 16 | </p> |
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| 17 | <ul> |
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| 18 | <li> <a href=\"Modelica://Modelica.Media.IdealGases\">Ideal gases:</a><br> |
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| 19 | 1241 high precision gas models based on the |
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| 20 | NASA Glenn coefficients, plus ideal gas mixture models based |
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| 21 | on the same data.</li> |
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| 22 | <li> <a href=\"Modelica://Modelica.Media.Water\">Water models:</a><br> |
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| 23 | ConstantPropertyLiquidWater, WaterIF97 (high precision |
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| 24 | water model according to the IAPWS/IF97 standard)</li> |
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| 25 | <li> <a href=\"Modelica://Modelica.Media.Air\">Air models:</a><br> |
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| 26 | SimpleAir, DryAirNasa, and MoistAir</li> |
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| 27 | <li> <a href=\"Modelica://Modelica.Media.Incompressible\"> |
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| 28 | Incompressible media:</a><br> |
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| 29 | TableBased incompressible fluid models (properties are defined by tables rho(T), |
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| 30 | HeatCapacity_cp(T), etc.)</li> |
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| 31 | <li> <a href=\"Modelica://Modelica.Media.CompressibleLiquids\"> |
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| 32 | Compressible liquids:</a><br> |
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| 33 | Simple liquid models with linear compressibility</li> |
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| 34 | </ul> |
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| 35 | <p> |
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| 36 | The following parts are useful, when newly starting with this library: |
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| 37 | <ul> |
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| 38 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide\">Modelica.Media.UsersGuide</a>.</li> |
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| 39 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage\">Modelica.Media.UsersGuide.MediumUsage</a> |
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| 40 | describes how to use a medium model in a component model.</li> |
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| 41 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumDefinition\"> |
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| 42 | Modelica.Media.UsersGuide.MediumDefinition</a> |
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| 43 | describes how a new fluid medium model has to be implemented.</li> |
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| 44 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.ReleaseNotes\">Modelica.Media.UsersGuide.ReleaseNotes</a> |
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| 45 | summarizes the changes of the library releases.</li> |
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| 46 | <li> <a href=\"Modelica://Modelica.Media.Examples\">Modelica.Media.Examples</a> |
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| 47 | contains examples that demonstrate the usage of this library.</li> |
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| 48 | </ul> |
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| 49 | <p> |
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| 50 | Copyright © 1998-2007, Modelica Association. |
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| 51 | </p> |
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| 52 | <p> |
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| 53 | <i>This Modelica package is <b>free</b> software; it can be redistributed and/or modified |
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| 54 | under the terms of the <b>Modelica license</b>, see the license conditions |
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| 55 | and the accompanying <b>disclaimer</b> |
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| 56 | <a href=\"Modelica://Modelica.UsersGuide.ModelicaLicense\">here</a>.</i> |
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| 57 | </p><br> |
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| 58 | </HTML>"), |
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| 59 | conversion(from(version="0.795", script= |
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| 60 | "../ConvertFromModelica.Media_0.795.mos"))); |
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| 61 | |
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| 62 | |
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| 63 | package UsersGuide "User's Guide of Media Library" |
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| 64 | |
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| 65 | annotation (DocumentationClass=true, Documentation(info="<HTML> |
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| 66 | <p> |
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| 67 | Library <b>Modelica.Media</b> is a <b>free</b> Modelica package providing |
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| 68 | a standardized interface to fluid media models and specific |
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| 69 | media models based on this interface. |
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| 70 | A fluid medium model defines <b>algebraic</b> equations |
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| 71 | for the intensive thermodynamic variables used in the <b>mass</b> |
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| 72 | and <b>energy</b> balance of component models. Optionally, additional |
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| 73 | medium properties can be computed such as dynamic viscosity or thermal |
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| 74 | conductivity. Medium models are defined for <b>single</b> and |
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| 75 | <b>multiple substance</b> fluids with <b>one</b> and |
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| 76 | <b>multiple phases</b>. |
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| 77 | </p> |
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| 78 | <p> |
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| 79 | A large part of the library provides specific medium models |
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| 80 | that can be directly utilized. This library can be used in |
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| 81 | all types of Modelica fluid libraries that may have different connectors |
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| 82 | and design philosophies. It is particularily utilized |
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| 83 | in the Modelica_Fluid library (the Modelica_Fluid library is currently |
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| 84 | under development to provide 1D thermo-fluid flow components for |
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| 85 | single and multiple substance flow with one and multiple phases). |
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| 86 | The Modelica.Media library has the following |
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| 87 | main features: |
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| 88 | </p> |
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| 89 | <ul> |
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| 90 | <li> Balance equations and media model equations |
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| 91 | are decoupled. |
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| 92 | This means that the used medium model does usually not have an |
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| 93 | influence on how the balance equations are formulated. |
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| 94 | For example, the same balance equations are used for media |
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| 95 | that use pressure and temperature, or pressure and specific |
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| 96 | enthalpy as independent variables, as well as for |
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| 97 | incompressible and compressible media models. |
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| 98 | A Modelica tool will have enough information to |
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| 99 | generate as efficient code as a traditional |
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| 100 | (coupled) definition. This feature is described in more |
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| 101 | detail in section |
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| 102 | <a href=\"Modelica://Modelica.Media.UsersGuide.MediumDefinition.StaticStateSelection\">Static State Selection</a>.</li> |
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| 103 | <li> Optional variables, such as dynamic viscosity, are only computed if |
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| 104 | needed in the corresponding component.</li> |
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| 105 | <li> The independent variables of a medium model do not |
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| 106 | influence the definition of a fluid connector port. |
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| 107 | Especially, the media models are implemented in such a way |
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| 108 | that a connector may have the minimum number of independent |
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| 109 | medium variables in a connector and still get the same |
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| 110 | efficiency as if all medium variables are passed by the |
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| 111 | connector from one component to the next one (the latter |
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| 112 | approach has the restriction that a fluid port can only |
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| 113 | connect two components and not more). Note, the Modelica_Fluid |
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| 114 | library uses the first approach, i.e., having a set of |
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| 115 | independent medium variables in a connector.</li> |
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| 116 | <li> The medium models are implemented with regards to |
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| 117 | efficient dynamic simulation. For example, two phase |
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| 118 | medium models trigger state events at phase boundaries |
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| 119 | (because the medium variables are not differentiable |
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| 120 | at this point).</li> |
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| 121 | </ul> |
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| 122 | <p> |
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| 123 | This User's Guide has the following main parts: |
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| 124 | </p> |
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| 125 | <ul> |
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| 126 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage\">Medium usage</a> |
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| 127 | describes how to use a medium model from |
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| 128 | this library in a component model.</li> |
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| 129 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumDefinition\">Medium definition</a> |
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| 130 | describes how a new fluid medium |
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| 131 | model has to be implemented.</li> |
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| 132 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.ReleaseNotes\">ReleaseNotes</a> |
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| 133 | summarizes the changes of the library releases.</li> |
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| 134 | <li><a href=\"Modelica://Modelica.Media.UsersGuide.Contact\">Contact</a> |
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| 135 | provides information about the authors of the library as well as |
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| 136 | acknowledgements.</li> |
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| 137 | </ul> |
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| 138 | </HTML>")); |
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| 139 | |
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| 140 | package MediumUsage "Medium usage" |
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| 141 | |
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| 142 | annotation (DocumentationClass=true, Documentation(info="<HTML> |
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| 143 | <p> |
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| 144 | Content: |
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| 145 | </p> |
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| 146 | <ol> |
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| 147 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage.BasicUsage\"> |
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| 148 | Basic usage of medium model</a></li> |
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| 149 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage.BalanceVolume\"> |
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| 150 | Medium model for a balance volume</a></li> |
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| 151 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage.ShortPipe\"> |
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| 152 | Medium model for a pressure loss</a></li> |
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| 153 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage.OptionalProperties\"> |
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| 154 | Optional medium properties</a></li> |
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| 155 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage.Constants\"> |
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| 156 | Constants provided by medium model</a></li> |
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| 157 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage.TwoPhase\"> |
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| 158 | Two-phase media</a></li> |
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| 159 | <li> <a href=\"Modelica://Modelica.Media.UsersGuide.MediumUsage.Initialization\"> |
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| 160 | Initialization</a></li> |
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| 161 | </ol> |
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| 162 | |
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| 163 | <p> |
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| 164 | A good demonstration how to use the media from Modelica.Media is |
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| 165 | given in package Modelica.Media.Examples.Tests. Under |
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| 166 | <a href=\"Modelica://Modelica.Media.Examples.Tests.Components\"> |
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| 167 | Tests.Components</a> the most basic components of a Fluid library |
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| 168 | are defined. Under Tests.MediaTestModels these basic components are used to test |
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| 169 | all media models with some very simple piping networks. |
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| 170 | </p> |
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| 171 | |
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| 172 | </HTML>")); |
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| 173 | |
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| 174 | class BasicUsage "Basic usage" |
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| 175 | |
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| 176 | annotation (Documentation(info="<HTML> |
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| 177 | <h4>Basic usage of medium model</h4> |
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| 178 | <p> |
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| 179 | Media models in Modelica.Media are provided by packages, inheriting from the |
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| 180 | partial package Modelica.Media.Interfaces.PartialMedium. Every package defines: |
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| 181 | <ul> |
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| 182 | <li> Medium <b>constants</b> (such as the number of chemical substances, |
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| 183 | molecular data, critical properties, etc.). |
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| 184 | <li> A BaseProperties <b>model</b>, to compute the basic thermodynamic |
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| 185 | properties of the fluid; |
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| 186 | <li> <b>setState_XXX</b> functions to compute the thermodynamic state record from |
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| 187 | different input arguments (such as density, temperature, and composition which |
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| 188 | would be setState_dTX); |
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| 189 | <li> <b>Functions</b> to compute additional properties (such as saturation |
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| 190 | properties, viscosity, thermal conductivity, etc.). |
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| 191 | </ul> |
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| 192 | There are - as stated above - two different basic ways of using the Media library which |
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| 193 | will be described in more details in the following section. One way is to use the model BaseProperties. |
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| 194 | Every instance of BaseProperties for any medium model provides <b>3+nXi |
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| 195 | equations</b> for the following <b>5+nXi variables</b> that are declared in |
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| 196 | the medium model (nXi is the number of independent mass fractions, see |
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| 197 | explanation below): |
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| 198 | </p> |
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| 199 | <table border=1 cellspacing=0 cellpadding=2> |
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| 200 | <tr><td valign=\"top\"><b>Variable</b></td> |
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| 201 | <td valign=\"top\"><b>Unit</b></td> |
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| 202 | <td valign=\"top\"><b>Description</b></td></tr> |
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| 203 | <tr><td valign=\"top\">T</td> |
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| 204 | <td valign=\"top\">K</td> |
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| 205 | <td valign=\"top\">temperature</td></tr> |
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| 206 | <tr><td valign=\"top\">p</td> |
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| 207 | <td valign=\"top\">Pa</td> |
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| 208 | <td valign=\"top\">absolute pressure</td></tr> |
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| 209 | <tr><td valign=\"top\">d</td> |
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| 210 | <td valign=\"top\">kg/m^3</td> |
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| 211 | <td valign=\"top\">density</td></tr> |
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| 212 | <tr><td valign=\"top\">u</td> |
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| 213 | <td valign=\"top\">J/kg</td> |
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| 214 | <td valign=\"top\">specific internal energy</td></tr> |
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| 215 | <tr><td valign=\"top\">h</td> |
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| 216 | <td valign=\"top\">J/kg</td> |
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| 217 | <td valign=\"top\">specific enthalpy (h = u + p/d)</td></tr> |
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| 218 | <tr><td valign=\"top\">Xi[nXi]</td> |
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| 219 | <td valign=\"top\">kg/kg</td> |
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| 220 | <td valign=\"top\">independent mass fractions m_i/m</td></tr> |
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| 221 | <tr><td valign=\"top\">X[nX]</td> |
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| 222 | <td valign=\"top\">kg/kg</td> |
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| 223 | <td valign=\"top\">All mass fractions m_i/m. X is defined in BaseProperties by:<br> |
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| 224 | X = <b>if</b> reducedX <b>then</b> vector([Xi; 1-<b>sum</b>(Xi)]) |
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| 225 | <b>else</b> Xi </td></tr> |
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| 226 | </table> |
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| 227 | <p> |
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| 228 | <b>Two</b> variables out of p, d, h, or u, as well as the |
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| 229 | <b>mass fractions</b> Xi are the <b>independent</b> variables and the |
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| 230 | medium model basically provides equations to compute |
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| 231 | the remaining variables, including the full mass fraction vector X |
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| 232 | (more details to Xi and X are given further below). |
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| 233 | </p> |
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| 234 | <p> |
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| 235 | In a component, the most basic usage of a medium model is as follows |
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| 236 | </p> |
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| 237 | <pre> |
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| 238 | <b>model</b> Pump |
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| 239 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium |
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| 240 | \"Medium model\" <b>annotation</b> (choicesAllMatching = <b>true</b>); |
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| 241 | Medium.BaseProperties medium_a \"Medium properties at location a (e.g. port_a)\"; |
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| 242 | // Use medium variables (medium_a.p, medium_a.T, medium_a.h, ...) |
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| 243 | ... |
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| 244 | <b>end</b> Pump; |
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| 245 | </pre> |
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| 246 | <p> |
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| 247 | The second way is to use the setState_XXX functions to compute the thermodynamic state |
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| 248 | record from which all other thermodynamic state variables can be computed (see |
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| 249 | <a href=\"Modelica://Modelica.Media.UsersGuide.MediumDefinition.BasicDefinition\"> |
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| 250 | Basic definition of medium</a> for further details on ThermodynamicState). The setState_XXX functions |
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| 251 | accept either X or Xi (see explanation below) and will decide internally which of these two compositions |
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| 252 | is provided by the user. The four fundamental setState_XXX functions are provided in PartialMedium |
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| 253 | </p> |
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| 254 | <table border=1 cellspacing=0 cellpadding=2> |
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| 255 | <tr><td valign=\"top\"><b>Function</b></td> |
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| 256 | <td valign=\"top\"><b>Description</b></td> |
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| 257 | <td valign=\"top\"><b>Short-form for<br>single component medium</b></td></tr> |
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| 258 | <tr><td valign=\"top\">setState_dTX</td> |
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| 259 | <td valign=\"top\">computes ThermodynamicState from density, temperature, and composition X or Xi</td> |
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| 260 | <td valign=\"top\">setState_dT</td></tr> |
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| 261 | <tr><td valign=\"top\">setState_phX</td> |
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| 262 | <td valign=\"top\">computes ThermodynamicState from pressure, specific enthalpy, and composition X or Xi</td> |
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| 263 | <td valign=\"top\">setState_ph</td></tr> |
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| 264 | <tr><td valign=\"top\">setState_psX</td> |
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| 265 | <td valign=\"top\">computes ThermodynamicState from pressure, specific entropy, and composition X or Xi</td> |
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| 266 | <td valign=\"top\">setState_ps</td></tr> |
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| 267 | <tr><td valign=\"top\">setState_pTX</td> |
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| 268 | <td valign=\"top\">computes ThermodynamicState from pressure, temperature, and composition X or Xi</td> |
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| 269 | <td valign=\"top\">setState_pT</td></tr> |
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| 270 | </table> |
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| 271 | <p> |
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| 272 | The simple example that explained the basic usage of BaseProperties would then become |
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| 273 | <pre> |
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| 274 | <b>model</b> Pump |
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| 275 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium |
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| 276 | \"Medium model\" <b>annotation</b> (choicesAllMatching = <b>true</b>); |
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| 277 | Medium.ThermodynamicState state_a \"Thermodynamic state record at location a (e.g. port_a)\"; |
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| 278 | // Compute medium variables from thermodynamic state record (pressure(state_a), temperature(state_a), |
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| 279 | // specificEnthalpy(state_a), ...) |
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| 280 | ... |
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| 281 | <b>end</b> Pump; |
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| 282 | </pre> |
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| 283 | <p> |
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| 284 | All media models are directly or indirectly a subpackage of package |
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| 285 | Modelica.Media.Interfaces.PartialMedium. Therefore, |
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| 286 | a medium model in a component should inherit from this |
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| 287 | partial package. Via the annotation \"choicesAllMatching = true\" it |
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| 288 | is defined that the tool should display a selection box with |
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| 289 | all loaded packages that inherit from PartialMedium. An example |
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| 290 | is given in the next figure: |
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| 291 | </p> |
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| 292 | <IMG SRC=\"../Images/Media/UsersGuide/mediumMenu.png\" ALT=\"medium selection menu\"> |
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| 293 | <p> |
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| 294 | A selected medium model leads, e.g., to the following equation: |
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| 295 | </p> |
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| 296 | <pre> |
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| 297 | Pump pump(<b>redeclare package</b> Medium = Modelica.Media.Water.SimpleLiquidWater); |
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| 298 | </pre> |
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| 299 | <p> |
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| 300 | Usually, a medium model is associated with the variables of a |
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| 301 | fluid connector. Therefore, equations have to be defined in a model |
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| 302 | that relate the variables in the connector with the variables |
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| 303 | in the medium model: |
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| 304 | </p> |
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| 305 | <pre> |
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| 306 | <b>model</b> Pump |
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| 307 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium |
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| 308 | \"Medium model\" <b>annotation</b> (choicesAllMatching = <b>true</b>); |
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| 309 | Medium.BaseProperties medium_a \"Medium properties of port_a\"; |
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| 310 | // definition of the fluid port port_a |
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| 311 | ... |
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| 312 | <b>equation</b> |
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| 313 | medium.p = port_a.p; |
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| 314 | medium.h = port_a.h; |
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| 315 | medium.Xi = port_a.Xi; |
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| 316 | ... |
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| 317 | <b>end</b> Pump; |
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| 318 | </pre> |
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| 319 | in the case of using BaseProperties or |
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| 320 | <pre> |
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| 321 | <b>model</b> Pump |
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| 322 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium |
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| 323 | \"Medium model\" <b>annotation</b> (choicesAllMatching = <b>true</b>); |
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| 324 | Medium.ThermodynamicState state_a \"Thermodynamic state record of medium at port_a\"; |
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| 325 | // definition of the fluid port port_a |
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| 326 | ... |
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| 327 | <b>equation</b> |
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| 328 | state_a = Medium.setState_phX(port_a.p, port_a.h, port_a.Xi) // if port_a contains the variables |
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| 329 | // p, h, and Xi |
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| 330 | ... |
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| 331 | <b>end</b> Pump; |
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| 332 | </pre> |
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| 333 | in the case of using ThermodynamicState. |
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| 334 | <p> |
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| 335 | If a component model shall treat both single and multiple |
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| 336 | substance fluids, equations for the mass fractions have to be |
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| 337 | present (above: medium.Xi = port_a.Xi) in the model. According |
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| 338 | to the Modelica semantics, the equations of the mass fractions |
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| 339 | are ignored, if the dimension of Xi is zero, i.e., for a single-component |
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| 340 | medium. Note, by specific techniques sketched in section |
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| 341 | \"Medium definition\", the independent variables in the medium model |
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| 342 | need not to be the same as the variables in the connector and still |
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| 343 | get the same efficiency, as if the same variables would be used. |
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| 344 | </p> |
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| 345 | |
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| 346 | <p> |
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| 347 | If a fluid consists of a single |
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| 348 | substance, <b>nXi = 0</b> and the vector of mass fractions Xi is not |
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| 349 | present. If a fluid consists of nS substances, |
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| 350 | the medium model may define the number of independent |
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| 351 | mass fractions <b>nXi</b> to be <b>nS</b>, <b>nS-1</b>, or zero. |
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| 352 | In all cases, balance equations for nXi substances have to be |
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| 353 | given in the corresponding component (see discussion below). |
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| 354 | Note, that if nXi = nS, the constraint \"sum(Xi)=1\" between the mass |
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| 355 | fractions is <b>not</b> present in the model; in that case, it is necessary to |
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| 356 | provide consistent start values for Xi such that sum(Xi) = 1. |
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| 357 | </p> |
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| 358 | |
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| 359 | <p> |
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| 360 | The reason for this definition of Xi is that a fluid component library |
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| 361 | can be implemented by using only the independent mass fractions Xi and |
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| 362 | then via the medium it is defined how Xi is interpreted: |
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| 363 | </p> |
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| 364 | |
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| 365 | <ul> |
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| 366 | <li> If Xi = nS, then the constraint equation sum(X) = 1 is neglected |
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| 367 | during simulation. By making sure that the initial conditions of X |
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| 368 | fulfill this constraint, it can usually be guaranteed that small |
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| 369 | errors in sum(X) = 1 remain small although this constraint equation is |
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| 370 | not explicitly used during the simulation. This approach is usually useful |
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| 371 | if components of the mixture can become very small. If such a small |
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| 372 | quantity is computed via the equation 1 - sum(X[1:nX-1]), there might |
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| 373 | be large numerical errors and it is better to compute it via |
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| 374 | the corresponding balance equation.</li> |
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| 375 | <li> If Xi = nS-1, then the true independent mass fractions are used |
|---|
| 376 | in the fluid component and the last component of X is computed via |
|---|
| 377 | X[nX] = 1 - sum(Xi). This is useful for, e.g., MoistAir, where the |
|---|
| 378 | number of states should be as small as possible without introducing |
|---|
| 379 | numerical problems.</li> |
|---|
| 380 | <li> If Xi = 0, then the reference value of composition reference_X is |
|---|
| 381 | assumed. This case is useful to avoid composition states in all |
|---|
| 382 | the cases when the composition will always be constant, e.g. with |
|---|
| 383 | circuits having fixed composition sources. |
|---|
| 384 | </ul> |
|---|
| 385 | |
|---|
| 386 | <p> |
|---|
| 387 | The full vector of mass fractions <b>X[nX]</b> is computed in |
|---|
| 388 | PartialMedium.BaseProperties based on Xi, reference_X, and the information whether Xi = nS or nS-1. For single-substance media, nX = 0, so there's also no X vector. For multiple-substance media, nX = nS, and X always contains the full vector of mass fractions. In order to reduce confusion for the user of a fluid component library, \"Xi\" has the annotation \"Hide=true\", meaning, that this variable is not shown in the plot window. Only X is shown in the plot window and this vector always contains all mass fractions. |
|---|
| 389 | </p> |
|---|
| 390 | </HTML>")); |
|---|
| 391 | end BasicUsage; |
|---|
| 392 | |
|---|
| 393 | class BalanceVolume "Balance volume" |
|---|
| 394 | |
|---|
| 395 | annotation (Documentation(info="<HTML> |
|---|
| 396 | <p> |
|---|
| 397 | Fluid libraries usually have balance volume components with one fluid connector |
|---|
| 398 | port that fulfill the mass and energy balance and on a different grid components that |
|---|
| 399 | fulfill the momentum balance. A balance volume component, called junction |
|---|
| 400 | volume below, should be primarily implemented in the following way |
|---|
| 401 | (see also the implementation in |
|---|
| 402 | <a href=\"Modelica://Modelica.Media.Examples.Tests.Components.PortVolume\"> |
|---|
| 403 | Modelica.Media.Examples.Tests.Components.PortVolume</a>): |
|---|
| 404 | </p> |
|---|
| 405 | <pre> |
|---|
| 406 | <b>model</b> JunctionVolume |
|---|
| 407 | <b>import</b> SI=Modelica.SIunits; |
|---|
| 408 | <b>import</b> Modelica.Media.Examples.Tests.Components.FluidPort_a; |
|---|
| 409 | |
|---|
| 410 | <b>parameter</b> SI.Volume V = 1e-6 \"Fixed size of junction volume\"; |
|---|
| 411 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium |
|---|
| 412 | \"Medium model\" <b>annotation</b> (choicesAllMatching = <b>true</b>); |
|---|
| 413 | |
|---|
| 414 | FluidPort_a port(<b>redeclare package</b> Medium = Medium); |
|---|
| 415 | Medium.BaseProperties medium(preferredMediumStates = <b>true</b>); |
|---|
| 416 | |
|---|
| 417 | SI.Energy U \"Internal energy of junction volume\"; |
|---|
| 418 | SI.Mass M \"Mass of junction volume\"; |
|---|
| 419 | SI.Mass MX[Medium.nXi] \"Independent substance masses of junction volume\"; |
|---|
| 420 | <b>equation</b> |
|---|
| 421 | medium.p = port.p; |
|---|
| 422 | medium.h = port.h; |
|---|
| 423 | medium.Xi = port.Xi; |
|---|
| 424 | |
|---|
| 425 | M = V*medium.d; // mass of JunctionVolume |
|---|
| 426 | MX = M*medium.Xi; // mass fractions in JunctionVolume |
|---|
| 427 | U = M*medium.u; // internal energy in JunctionVolume |
|---|
| 428 | |
|---|
| 429 | <b>der</b>(M) = port.m_flow; // mass balance |
|---|
| 430 | <b>der</b>(MX) = port.mX_flow; // substance mass balance |
|---|
| 431 | <b>der</b>(U) = port.H_flow; // energy balance |
|---|
| 432 | <b>end</b> JunctionVolume; |
|---|
| 433 | </pre> |
|---|
| 434 | <p> |
|---|
| 435 | Assume the Modelica.Media.Air.SimpleAir medium model is used with |
|---|
| 436 | the JunctionVolume model above. This medium model uses pressure p |
|---|
| 437 | and temperature T as independent variables. If the flag |
|---|
| 438 | \"preferredMediumStates\" is set to <b>true</b> in the declaration |
|---|
| 439 | of \"medium\", then the independent variables of this medium model |
|---|
| 440 | get the attribute \"stateSelect = StateSelect.prefer\", i.e., the |
|---|
| 441 | Modelica translator should use these variables as states, if this |
|---|
| 442 | is possible. Basically, this means that |
|---|
| 443 | constraints between the |
|---|
| 444 | potential states p,T and the potential states U,M are present. |
|---|
| 445 | A Modelica tool will therefore <b>automatically</b> |
|---|
| 446 | differentiate medium equations and will use the following |
|---|
| 447 | equations for code generation (note the equations related to X are |
|---|
| 448 | removed, because SimpleAir consists of a single substance only): |
|---|
| 449 | </p> |
|---|
| 450 | <pre> |
|---|
| 451 | M = V*medium.d; |
|---|
| 452 | U = M*medium.u; |
|---|
| 453 | |
|---|
| 454 | // balance equations |
|---|
| 455 | <b>der</b>(M) = port.m_flow; |
|---|
| 456 | <b>der</b>(U) = port.H_flow; |
|---|
| 457 | |
|---|
| 458 | // abbreviations introduced to get simpler terms |
|---|
| 459 | p = medium.p; |
|---|
| 460 | T = medium.T; |
|---|
| 461 | d = medium.d; |
|---|
| 462 | u = medium.u; |
|---|
| 463 | h = medium.h; |
|---|
| 464 | |
|---|
| 465 | // medium equations |
|---|
| 466 | d = fd(p,T); |
|---|
| 467 | h = fh(p,T); |
|---|
| 468 | u = h - p/d; |
|---|
| 469 | |
|---|
| 470 | // equations derived <b>automatically</b> by a Modelica tool due to index reduction |
|---|
| 471 | <b>der</b>(U) = <b>der</b>(M)*u + M*<b>der</b>(u); |
|---|
| 472 | <b>der</b>(M) = V*<b>der</b>(d); |
|---|
| 473 | <b>der</b>(u) = <b>der</b>(h) - <b>der</b>(p)/d - p/<b>der</b>(d); |
|---|
| 474 | <b>der</b>(d) = <b>der</b>(fd,p)*<b>der</b>(p) + <b>der</b>(fd,T)*<b>der</b>(T); |
|---|
| 475 | <b>der</b>(h) = <b>der</b>(fh,p)*<b>der</b>(p) + <b>der</b>(fd,T)*<b>der</b>(T); |
|---|
| 476 | </pre> |
|---|
| 477 | <p> |
|---|
| 478 | Note, that \"der(y,x)\" is an operator that characterizes |
|---|
| 479 | in the example above the partial derivative of y with respect to x |
|---|
| 480 | (this operator will be included in one of the next Modelica language |
|---|
| 481 | releases). |
|---|
| 482 | All media models in this library are written in such a way that |
|---|
| 483 | at least the partial derivatives of the medium variables with |
|---|
| 484 | respect to the independent variables are provided, either because |
|---|
| 485 | the equations are directly given (= symbolic differentiation is possible) |
|---|
| 486 | or because the derivative of the corresponding function (such as fd above) |
|---|
| 487 | is provided. A Modelica tool will transform the equations above |
|---|
| 488 | in differential equations with p and T as states, i.e., will |
|---|
| 489 | generate equations to compute <b>der</b>(p) and <b>der</b>(T) as function of p and T. |
|---|
| 490 | </p> |
|---|
| 491 | |
|---|
| 492 | <p> |
|---|
| 493 | Note, when preferredMediumStates = <b>false</b>, no differentiation |
|---|
| 494 | will take place and the Modelica translator will use the variables |
|---|
| 495 | appearing differentiated as states, i.e., M and U. This has the |
|---|
| 496 | disadvantage that for many media non-linear systems of equations are |
|---|
| 497 | present to compute the intrinsic properties p, d, T, u, h from |
|---|
| 498 | M and U. |
|---|
| 499 | </p> |
|---|
| 500 | </HTML>")); |
|---|
| 501 | end BalanceVolume; |
|---|
| 502 | |
|---|
| 503 | class ShortPipe "Short pipe" |
|---|
| 504 | |
|---|
| 505 | annotation (Documentation(info="<HTML> |
|---|
| 506 | <p> |
|---|
| 507 | Fluid libraries have components with two ports that store |
|---|
| 508 | neither mass nor energy and fulfill the |
|---|
| 509 | momentum equation between their two ports, e.g., a short pipe. In most |
|---|
| 510 | cases this means that an equation is present relating the pressure |
|---|
| 511 | drop between the two ports and the mass flow rate from one to the |
|---|
| 512 | other port. Since no mass or energy is stored, no differential |
|---|
| 513 | equations for thermodynamic variables are present. A component model of this type |
|---|
| 514 | has therefore usually the following structure |
|---|
| 515 | (see also the implementation in |
|---|
| 516 | <a href=\"Modelica://Modelica.Media.Examples.Tests.Components.ShortPipe\"> |
|---|
| 517 | Modelica.Media.Examples.Tests.Components.ShortPipe</a>): |
|---|
| 518 | </p> |
|---|
| 519 | <pre> |
|---|
| 520 | <b>model</b> ShortPipe |
|---|
| 521 | <b>import</b> SI=Modelica.SIunits; |
|---|
| 522 | <b>import</b> Modelica.Media.Examples.Tests.Components; |
|---|
| 523 | |
|---|
| 524 | // parameters defining the pressure drop equation |
|---|
| 525 | |
|---|
| 526 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium |
|---|
| 527 | \"Medium model\" <b>annotation</b> (choicesAllMatching = <b>true</b>); |
|---|
| 528 | |
|---|
| 529 | Component.FluidPort_a port_a (<b>redeclare package</b> Medium = Medium); |
|---|
| 530 | Component.FluidPort_b port_b (<b>redeclare package</b> Medium = Medium); |
|---|
| 531 | |
|---|
| 532 | SI.Pressure dp = port_a.p - port_b.p \"Pressure drop\"; |
|---|
| 533 | Medium.BaseProperties medium_a \"Medium properties in port_a\"; |
|---|
| 534 | Medium.BasePropreties medium_b \"Medium properties in port_b\"; |
|---|
| 535 | <b>equation</b> |
|---|
| 536 | // define media models of the ports |
|---|
| 537 | medium_a.p = port_a.p; |
|---|
| 538 | medium_a.h = port_a.h; |
|---|
| 539 | medium_a.Xi = port_a.Xi; |
|---|
| 540 | |
|---|
| 541 | medium_b.p = port_b.p; |
|---|
| 542 | medium_b.h = port_b.h; |
|---|
| 543 | medium_b.Xi = port_b.Xi; |
|---|
| 544 | |
|---|
| 545 | // Handle reverse and zero flow (semiLinear is a built-in Modelica operator) |
|---|
| 546 | port_a.H_flow = <b>semiLinear</b>(port_a.m_flow, port_a.h, port_b.h); |
|---|
| 547 | port_a.mXi_flow = <b>semiLinear</b>(port_a.m_flow, port_a.Xi, port_b.Xi); |
|---|
| 548 | |
|---|
| 549 | // Energy, mass and substance mass balance |
|---|
| 550 | port_a.H_flow + port_b.H_flow = 0; |
|---|
| 551 | port_a.m_flow + port_b.m_flow = 0; |
|---|
| 552 | port_a.mXi_flow + port_b.mXi_flow = zeros(Medium.nXi); |
|---|
| 553 | |
|---|
| 554 | // Provide equation: port_a.m_flow = f(dp) |
|---|
| 555 | <b>end</b> ShortPipe; |
|---|
| 556 | </pre> |
|---|
| 557 | |
|---|
| 558 | <p> |
|---|
| 559 | The <b>semiLinear</b>(..) operator is basically defined as: |
|---|
| 560 | </p> |
|---|
| 561 | <pre> |
|---|
| 562 | semiLinear(m_flow, ha, hb) = if m_flow ≥ 0 then m_flow*ha else m_flow*hb; |
|---|
| 563 | </pre> |
|---|
| 564 | |
|---|
| 565 | <p> |
|---|
| 566 | that is, it computes the enthalpy flow rate either from the port_a or |
|---|
| 567 | from the port_b properties, depending on flow direction. The exact |
|---|
| 568 | details of this operator are given in |
|---|
| 569 | <a href=\"Modelica://ModelicaReference.Operators.SemiLinear\"> |
|---|
| 570 | ModelicaReference.Operators.SemiLinear</a>. Especially, rules |
|---|
| 571 | are defined in the Modelica specification that m_flow = 0 can be treated |
|---|
| 572 | in a \"meaningful way\". Especially, if n fluid components (such as pipes) |
|---|
| 573 | are connected together and the fluid connector from above is used, |
|---|
| 574 | a linear system of equations appear between |
|---|
| 575 | medium1.h, medium2.h, medium3.h, ..., port1.h, port2.h, port3.h, ..., |
|---|
| 576 | port1.H_flow, port2.H_flow, port3.H_flow, .... The rules for the |
|---|
| 577 | semiLinear(..) operator allow the following solution of this |
|---|
| 578 | linear system of equations: |
|---|
| 579 | </p> |
|---|
| 580 | |
|---|
| 581 | <ul> |
|---|
| 582 | <li> n = 2 (two components are connected):<br> |
|---|
| 583 | The linear system of equations can be analytically solved |
|---|
| 584 | with the result |
|---|
| 585 | <pre> |
|---|
| 586 | medium1.h = medium2.h = port1.h = port2.h |
|---|
| 587 | 0 = port1.H_flow + port2.H_flow |
|---|
| 588 | </pre> |
|---|
| 589 | Therefore, no problems with zero mass flow rate are present.</li> |
|---|
| 590 | |
|---|
| 591 | <li> n > 2 (more than two components are connected together):<br> |
|---|
| 592 | The linear system of equations is solved numerically during simulation. |
|---|
| 593 | For m_flow = 0, the linear system becomes singular and has an |
|---|
| 594 | infinite number of solutions. The simulator could use the solution t |
|---|
| 595 | that is closest to the solution in the previous time step |
|---|
| 596 | (\"least squares solution\"). Physically, the solution is determined |
|---|
| 597 | by diffusion which is usually neglected. If diffusion is included, |
|---|
| 598 | the linear system is regular.</li> |
|---|
| 599 | </ul> |
|---|
| 600 | |
|---|
| 601 | </HTML>")); |
|---|
| 602 | end ShortPipe; |
|---|
| 603 | |
|---|
| 604 | class OptionalProperties "Optional properties" |
|---|
| 605 | |
|---|
| 606 | annotation (Documentation(info="<HTML> |
|---|
| 607 | <p> |
|---|
| 608 | In some cases additional medium properties are needed. |
|---|
| 609 | A component that needs these optional properties has to call |
|---|
| 610 | one of the functions listed in the following table. They are |
|---|
| 611 | defined as partial functions within package |
|---|
| 612 | <a href=\"Modelica://Modelica.Media.Interfaces.PartialMedium\">PartialMedium</a>, |
|---|
| 613 | and then (optionally) implemented in actual medium packages. |
|---|
| 614 | If a component calls such an optional function and the |
|---|
| 615 | medium package does not provide a new implementation for this |
|---|
| 616 | function, an error message is printed at translation time, |
|---|
| 617 | since the function is \"partial\", i.e., incomplete. |
|---|
| 618 | The argument of all functions is the <b>state</b> record, |
|---|
| 619 | automatically defined by the BaseProperties model or specifically computed using the |
|---|
| 620 | setState_XXX functions, which contains the |
|---|
| 621 | minimum number of thermodynamic variables needed to compute all the additional |
|---|
| 622 | properties. In the table it is assumed that there is a declaration of the |
|---|
| 623 | form: |
|---|
| 624 | </p> |
|---|
| 625 | <pre> |
|---|
| 626 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium; |
|---|
| 627 | Medium.ThermodynamicState state; |
|---|
| 628 | </pre> |
|---|
| 629 | <table border=1 cellspacing=0 cellpadding=2> |
|---|
| 630 | <tr><td valign=\"top\"><b>Function call</b></td> |
|---|
| 631 | <td valign=\"top\"><b>Unit</b></td> |
|---|
| 632 | <td valign=\"top\"><b>Description</b></td></tr> |
|---|
| 633 | <tr><td valign=\"top\">Medium.dynamicViscosity(state)</b></td> |
|---|
| 634 | <td valign=\"top\">Pa.s</td> |
|---|
| 635 | <td valign=\"top\">dynamic viscosity</td></tr> |
|---|
| 636 | <tr><td valign=\"top\">Medium.thermalConductivity(state)</td> |
|---|
| 637 | <td valign=\"top\">W/(m.K)</td> |
|---|
| 638 | <td valign=\"top\">thermal conductivity</td></tr> |
|---|
| 639 | <tr><td valign=\"top\">Medium.prandtlNumber(state)</td> |
|---|
| 640 | <td valign=\"top\">1</td> |
|---|
| 641 | <td valign=\"top\">Prandtl number</td></tr> |
|---|
| 642 | <tr><td valign=\"top\">Medium.specificEntropy(state)</td> |
|---|
| 643 | <td valign=\"top\">J/(kg.K)</td> |
|---|
| 644 | <td valign=\"top\">specific entropy</td></tr> |
|---|
| 645 | <tr><td valign=\"top\">Medium.specificHeatCapacityCp(state)</td> |
|---|
| 646 | <td valign=\"top\">J/(kg.K)</td> |
|---|
| 647 | <td valign=\"top\">specific heat capacity at constant pressure</td></tr> |
|---|
| 648 | <tr><td valign=\"top\">Medium.specificHeatCapacityCv(state)</td> |
|---|
| 649 | <td valign=\"top\">J/(kg.K)</td> |
|---|
| 650 | <td valign=\"top\">specific heat capacity at constant density</td></tr> |
|---|
| 651 | <tr><td valign=\"top\">Medium.isentropicExponent(state)</td> |
|---|
| 652 | <td valign=\"top\">1</td> |
|---|
| 653 | <td valign=\"top\">isentropic exponent</td></tr> |
|---|
| 654 | <tr><td valign=\"top\">Medium.isentropicEnthatlpy(pressure, state)</td> |
|---|
| 655 | <td valign=\"top\">J/kg</td> |
|---|
| 656 | <td valign=\"top\">isentropic enthalpy</td></tr> |
|---|
| 657 | <tr><td valign=\"top\">Medium.velocityOfSound(state)</td> |
|---|
| 658 | <td valign=\"top\">m/s</td> |
|---|
| 659 | <td valign=\"top\">velocity of sound</td></tr> |
|---|
| 660 | <tr><td valign=\"top\">Medium.isobaricExpansionCoefficient(state)</td> |
|---|
| 661 | <td valign=\"top\">1/K</td> |
|---|
| 662 | <td valign=\"top\">isobaric expansion coefficient</td></tr> |
|---|
| 663 | <tr><td valign=\"top\">Medium.isothermalCompressibility(state)</td> |
|---|
| 664 | <td valign=\"top\">1/Pa</td> |
|---|
| 665 | <td valign=\"top\">isothermal compressibility</td></tr> |
|---|
| 666 | <tr><td valign=\"top\">Medium.density_derp_h(state)</td> |
|---|
| 667 | <td valign=\"top\">kg/(m3.Pa)</td> |
|---|
| 668 | <td valign=\"top\">derivative of density by pressure at constant enthalpy</td></tr> |
|---|
| 669 | <tr><td valign=\"top\">Medium.density_derh_p(state)</td> |
|---|
| 670 | <td valign=\"top\">kg2/(m3.J)</td> |
|---|
| 671 | <td valign=\"top\">derivative of density by enthalpy at constant pressure</td></tr> |
|---|
| 672 | <tr><td valign=\"top\">Medium.density_derp_T(state)</td> |
|---|
| 673 | <td valign=\"top\">kg/(m3.Pa)</td> |
|---|
| 674 | <td valign=\"top\">derivative of density by pressure at constant temperature</td></tr> |
|---|
| 675 | <tr><td valign=\"top\">Medium.density_derT_p(state)</td> |
|---|
| 676 | <td valign=\"top\">kg/(m3.K)</td> |
|---|
| 677 | <td valign=\"top\">derivative of density by temperature at constant pressure</td></tr> |
|---|
| 678 | <tr><td valign=\"top\">Medium.density_derX(state)</td> |
|---|
| 679 | <td valign=\"top\">kg/m3</td> |
|---|
| 680 | <td valign=\"top\">derivative of density by mass fraction</td></tr> |
|---|
| 681 | <tr><td valign=\"top\">Medium.molarMass(state)</td> |
|---|
| 682 | <td valign=\"top\">kg/mol</td> |
|---|
| 683 | <td valign=\"top\">molar mass</td></tr> |
|---|
| 684 | </table> |
|---|
| 685 | <p> |
|---|
| 686 | There are also some short forms provided for user convenience that allow the computation of certain |
|---|
| 687 | thermodynamic state variables without using the ThermodynamicState record explicitly. Those short forms |
|---|
| 688 | are for example useful to compute consistent start values in the initial equation section. Let's |
|---|
| 689 | consider the function temperature_phX(p,h,X) as an exmaple. This function computes the temperature |
|---|
| 690 | from pressure, specific enthalpy, and composition X (or Xi) and is a short form for writing |
|---|
| 691 | </p> |
|---|
| 692 | <pre> |
|---|
| 693 | temperature(setState_phX(p,h,X)) |
|---|
| 694 | </pre> |
|---|
| 695 | <p> |
|---|
| 696 | The following functions are predefined in PartialMedium (other functions can be added in the actual |
|---|
| 697 | medium implementation package if they are useful) |
|---|
| 698 | </p> |
|---|
| 699 | <table border=1 cellspacing=0 cellpadding=2> |
|---|
| 700 | <tr><td valign=\"top\">Medium.specificEnthalpy_pTX(p,T,X)</td> |
|---|
| 701 | <td valign=\"top\">J/kg</td> |
|---|
| 702 | <td valign=\"top\">Specific enthalpy at p, T, X </td></tr> |
|---|
| 703 | <tr><td valign=\"top\">Medium.temperature_phX(p,h,X)</td> |
|---|
| 704 | <td valign=\"top\">K</td> |
|---|
| 705 | <td valign=\"top\">Temperature at p, h, X</td></tr> |
|---|
| 706 | <tr><td valign=\"top\">Medium.density_phX(p,h,X)</td> |
|---|
| 707 | <td valign=\"top\">kg/m³</td> |
|---|
| 708 | <td valign=\"top\">Density at p, h, X</td></tr> |
|---|
| 709 | <tr><td valign=\"top\">Medium.temperature_psX(p,s,X)</td> |
|---|
| 710 | <td valign=\"top\">K</td> |
|---|
| 711 | <td valign=\"top\">Temperature at p, s, X</td></tr> |
|---|
| 712 | <tr><td valign=\"top\">Medium.specificEnthalpy_psX(p,s,X)</td> |
|---|
| 713 | <td valign=\"top\">J/(kg.K)</td> |
|---|
| 714 | <td valign=\"top\">Specific entropy at p, s, X</td></tr> |
|---|
| 715 | </table> |
|---|
| 716 | <p> |
|---|
| 717 | Assume for example that the dynamic viscosity eta is needed in |
|---|
| 718 | the pressure drop equation of a short pipe. Then, the |
|---|
| 719 | model of a short pipe has to be changed to: |
|---|
| 720 | </p> |
|---|
| 721 | <pre> |
|---|
| 722 | <b>model</b> ShortPipe |
|---|
| 723 | ... |
|---|
| 724 | Medium.BaseProperties medium_a \"Medium properties in port_a\"; |
|---|
| 725 | Medium.BaseProperties medium_b \"Medium properties in port_b\"; |
|---|
| 726 | ... |
|---|
| 727 | Medium.DynamicViscosity eta; |
|---|
| 728 | ... |
|---|
| 729 | eta = <b>if</b> port_a.m_flow > 0 <b>then</b> |
|---|
| 730 | Medium.dynamicViscosity(medium_a.state) |
|---|
| 731 | <b>else</b> |
|---|
| 732 | Medium.dynamicViscosity(medium_b.state); |
|---|
| 733 | // use eta in the pressure drop equation: port_a.m_flow = f(dp, eta) |
|---|
| 734 | <b>end</b> ShortPipe; |
|---|
| 735 | </pre> |
|---|
| 736 | |
|---|
| 737 | <p> |
|---|
| 738 | Note, \"Medium.DynamicViscosity\" is a type defined in Modelica.Interfaces.PartialMedium |
|---|
| 739 | as |
|---|
| 740 | </p> |
|---|
| 741 | |
|---|
| 742 | <pre> |
|---|
| 743 | <b>import</b> SI = Modelica.SIunits; |
|---|
| 744 | <b>type</b> DynamicViscosity = SI.DynamicViscosity ( |
|---|
| 745 | min=0, |
|---|
| 746 | max=1.e8, |
|---|
| 747 | nominal=1.e-3, |
|---|
| 748 | start=1.e-3); |
|---|
| 749 | </pre> |
|---|
| 750 | |
|---|
| 751 | <p> |
|---|
| 752 | Every medium model may modify the attributes, to provide, e.g., |
|---|
| 753 | min, max, nominal, and start values adapted to the medium. |
|---|
| 754 | Also, other types, such as AbsolutePressure, Density, MassFlowRate, |
|---|
| 755 | etc. are defined in PartialMedium. Whenever possible, these medium |
|---|
| 756 | specific types should be used in a model in order that medium information, |
|---|
| 757 | e.g., about nominal or start values, are automatically utilized. |
|---|
| 758 | </p> |
|---|
| 759 | |
|---|
| 760 | </pre> |
|---|
| 761 | |
|---|
| 762 | </HTML>")); |
|---|
| 763 | end OptionalProperties; |
|---|
| 764 | |
|---|
| 765 | class Constants "Constants" |
|---|
| 766 | |
|---|
| 767 | annotation (Documentation(info="<HTML> |
|---|
| 768 | <p> |
|---|
| 769 | Every medium model provides the following <b>constants</b>. For example, |
|---|
| 770 | if a medium is declared as: |
|---|
| 771 | </p> |
|---|
| 772 | <pre> |
|---|
| 773 | <b>replaceable package</b> Medium = Modelica.Media.Interfaces.PartialMedium; |
|---|
| 774 | </pre> |
|---|
| 775 | <p> |
|---|
| 776 | then constants \"Medium.mediumName\", \"Medium.nX\", etc. are defined: |
|---|
| 777 | </p> |
|---|
| 778 | <table border=1 cellspacing=0 cellpadding=2> |
|---|
| 779 | <tr><td valign=\"top\"><b>Type</b></td> |
|---|
| 780 | <td valign=\"top\"><b>Name</b></td> |
|---|
| 781 | <td valign=\"top\"><b>Description</b></td></tr> |
|---|
| 782 | <tr><td valign=\"top\">String</td><td valign=\"top\">mediumName</td> |
|---|
| 783 | <td valign=\"top\">Unique name of the medium (is usually used to check whether |
|---|
| 784 | the media in different components connected together |
|---|
| 785 | are the same, by providing Medium.mediumName as quantity |
|---|
| 786 | attribute of the mass flow rate in the connector)</td></tr> |
|---|
| 787 | <tr><td valign=\"top\">String</td><td valign=\"top\">substanceNames[nS]</td> |
|---|
| 788 | <td valign=\"top\">Names of the substances that make up the medium. |
|---|
| 789 | If only one substance is present, substanceNames = {mediumName}.</td></tr> |
|---|
| 790 | <tr><td valign=\"top\">String</td><td valign=\"top\">extraPropertiesNames[nC]</td> |
|---|
| 791 | <td valign=\"top\">Names of the extra transported substances, outside of mass and |
|---|
| 792 | energy balances.</td></tr> |
|---|
| 793 | <tr><td valign=\"top\">Boolean</td><td valign=\"top\">singleState</td> |
|---|
| 794 | <td valign=\"top\">= <b>true</b>, if u and d are not a function of pressure, and thus only |
|---|
| 795 | a function of a single thermal variable (temperature or enthalpy) and |
|---|
| 796 | of Xi for a multiple substance medium. Usually, this flag is |
|---|
| 797 | <b>true</b> for incompressible media. It is used in a model to determine |
|---|
| 798 | whether 1+nXi (singleState=<b>true</b>) or 2+nXi (singleState=<b>false</b>) |
|---|
| 799 | initial conditions have to be provided for a volume element that |
|---|
| 80 |
|---|