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Failed
tests / 04 testsuite-clang 1/3 / openmodelica_cppruntime_fmu_modelExchange_2.0.testDrumBoiler.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ testDrumBoiler ... equation mismatch [time: 52]
==== Log /tmp/omc-rtest-unknown/openmodelica/cppruntime/fmu/modelExchange/2.0/testDrumBoiler.mos_temp5065/log-testDrumBoiler.mos
true
""
true
""
true
""
true
""
"DrumBoilerModel.fmu"
"Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
"
0
"<?xml version=\"1.0\" encoding=\"UTF-8\"?>
<fmiModelDescription
fmiVersion=\"2.0\"
modelName=\"DrumBoilerModel\"
description=\"\"
variableNamingConvention=\"structured\"
numberOfEventIndicators=\"3\">
<ModelExchange
modelIdentifier=\"DrumBoilerModel\" providesDirectionalDerivative=\"true\">
</ModelExchange>
<UnitDefinitions>
<Unit name=\"m/s2\">
<BaseUnit m=\"1\" s=\"-2\" />
</Unit>
<Unit name=\"1/K\">
<BaseUnit K=\"-1\" />
</Unit>
<Unit name=\"s\">
<BaseUnit s=\"1\" />
</Unit>
<Unit name=\"kg/(s.Pa)\">
<BaseUnit m=\"1\" s=\"1\" />
</Unit>
<Unit name=\"1\">
<BaseUnit />
</Unit>
<Unit name=\"N/mm2\">
<BaseUnit m=\"-1\" s=\"-2\" kg=\"1\" factor=\"1e6\" />
</Unit>
<Unit name=\"MW\">
<BaseUnit m=\"2\" s=\"-3\" kg=\"1\" factor=\"1e6\" />
</Unit>
<Unit name=\"bar\">
<BaseUnit m=\"-1\" s=\"-2\" kg=\"1\" factor=\"1e5\" />
</Unit>
<Unit name=\"kg/kg\">
<BaseUnit />
</Unit>
<Unit name=\"degC\">
<BaseUnit K=\"1\" />
</Unit>
<Unit name=\"J/(kg.K)\">
<BaseUnit m=\"2\" s=\"-2\" K=\"-1\" />
</Unit>
<Unit name=\"kg/mol\">
<BaseUnit mol=\"-1\" kg=\"1\" />
</Unit>
<Unit name=\"kg/s\">
<BaseUnit s=\"-1\" kg=\"1\" />
</Unit>
<Unit name=\"kg/m3\">
<BaseUnit m=\"-3\" kg=\"1\" />
</Unit>
<Unit name=\"W\">
<BaseUnit m=\"2\" s=\"-3\" kg=\"1\" />
</Unit>
<Unit name=\"kg\">
<BaseUnit kg=\"1\" />
</Unit>
<Unit name=\"J/kg\">
<BaseUnit m=\"2\" s=\"-2\" />
</Unit>
<Unit name=\"J\">
<BaseUnit m=\"2\" s=\"-2\" kg=\"1\" />
</Unit>
<Unit name=\"m3/s\">
<BaseUnit m=\"3\" s=\"-1\" />
</Unit>
<Unit name=\"K\">
<BaseUnit K=\"1\" />
</Unit>
<Unit name=\"km-1.s-3.g\">
<BaseUnit m=\"-1\" s=\"-3\" kg=\"1\" factor=\"1e-6\" />
</Unit>
<Unit name=\"m3.s-1\">
<BaseUnit m=\"3\" s=\"-1\" />
</Unit>
<Unit name=\"Pa\">
<BaseUnit m=\"-1\" s=\"-2\" kg=\"1\" />
</Unit>
<Unit name=\"m3\">
<BaseUnit m=\"3\" />
</Unit>
</UnitDefinitions>
<TypeDefinitions>
<SimpleType name=\"Modelica.Blocks.Types.Init\">
<Enumeration>
<Item name=\"NoInit\" value=\"1\"/>
<Item name=\"SteadyState\" value=\"2\"/>
<Item name=\"InitialState\" value=\"3\"/>
<Item name=\"InitialOutput\" value=\"4\"/>
</Enumeration>
</SimpleType>
<SimpleType name=\"Modelica.Fluid.Types.Dynamics\">
<Enumeration>
<Item name=\"DynamicFreeInitial\" value=\"1\"/>
<Item name=\"FixedInitial\" value=\"2\"/>
<Item name=\"SteadyStateInitial\" value=\"3\"/>
<Item name=\"SteadyState\" value=\"4\"/>
</Enumeration>
</SimpleType>
<SimpleType name=\"Modelica.Fluid.Types.PortFlowDirection\">
<Enumeration>
<Item name=\"Entering\" value=\"1\"/>
<Item name=\"Leaving\" value=\"2\"/>
<Item name=\"Bidirectional\" value=\"3\"/>
</Enumeration>
</SimpleType>
</TypeDefinitions>
<LogCategories>
<Category name=\"logEvents\" />
<Category name=\"logSingularLinearSystems\" />
<Category name=\"logNonlinearSystems\" />
<Category name=\"logDynamicStateSelection\" />
<Category name=\"logStatusWarning\" />
<Category name=\"logStatusDiscard\" />
<Category name=\"logStatusError\" />
<Category name=\"logStatusFatal\" />
<Category name=\"logStatusPending\" />
<Category name=\"logAll\" />
<Category name=\"logFmi2Call\" />
</LogCategories>
<DefaultExperiment startTime=\"0.0\" stopTime=\"1.0\" tolerance=\"1e-6\"/>
<ModelVariables>
<!-- Index of variable = \"1\" -->
<ScalarVariable
name=\"controller.x\"
valueReference=\"0\"
description=\"State of block\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"2\" -->
<ScalarVariable
name=\"evaporator.V_l\"
valueReference=\"1\"
description=\"volumes of liquid phase\"
>
<Real unit=\"m3\"/>
</ScalarVariable>
<!-- Index of variable = \"3\" -->
<ScalarVariable
name=\"evaporator.p\"
valueReference=\"2\"
description=\"pressure inside drum boiler\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"4\" -->
<ScalarVariable
name=\"der(controller.x)\"
valueReference=\"3\"
description=\"der(State of block)\"
>
<Real derivative=\"1\"/>
</ScalarVariable>
<!-- Index of variable = \"5\" -->
<ScalarVariable
name=\"der(evaporator.V_l)\"
valueReference=\"4\"
description=\"der(volumes of liquid phase)\"
initial=\"approx\">
<Real start=\"0.0\" derivative=\"2\" nominal=\"500.0\" unit=\"m3.s-1\"/>
</ScalarVariable>
<!-- Index of variable = \"6\" -->
<ScalarVariable
name=\"der(evaporator.p)\"
valueReference=\"5\"
description=\"der(pressure inside drum boiler)\"
initial=\"approx\">
<Real start=\"0.0\" derivative=\"3\" nominal=\"5e8\" unit=\"km-1.s-3.g\"/>
</ScalarVariable>
<!-- Index of variable = \"7\" -->
<ScalarVariable
name=\"der(evaporator.T_D)\"
valueReference=\"6\"
description=\"temperature of drum\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"8\" -->
<ScalarVariable
name=\"der(evaporator.U)\"
valueReference=\"7\"
description=\"internal energy\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"9\" -->
<ScalarVariable
name=\"der(evaporator.V_v)\"
valueReference=\"8\"
description=\"volume of vapour phase\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"10\" -->
<ScalarVariable
name=\"der(evaporator.h_l)\"
valueReference=\"9\"
description=\"specific enthalpy of liquid\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"11\" -->
<ScalarVariable
name=\"der(evaporator.h_v)\"
valueReference=\"10\"
description=\"specific enthalpy of vapour\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"12\" -->
<ScalarVariable
name=\"der(evaporator.m)\"
valueReference=\"11\"
description=\"total mass of drum boiler\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"13\" -->
<ScalarVariable
name=\"der(evaporator.rho_l)\"
valueReference=\"12\"
description=\"density in liquid phase\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"14\" -->
<ScalarVariable
name=\"der(evaporator.rho_v)\"
valueReference=\"13\"
description=\"density in vapour phase\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"15\" -->
<ScalarVariable
name=\"K2degC.Kelvin\"
valueReference=\"125\"
>
<Real min=\"0.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"16\" -->
<ScalarVariable
name=\"MW2W.y\"
valueReference=\"126\"
description=\"Output signal connector\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"17\" -->
<ScalarVariable
name=\"SteamValve.V_flow\"
valueReference=\"127\"
description=\"Volume flow rate at inflowing port (positive when flow from port_a to port_b)\"
>
<Real unit=\"m3/s\"/>
</ScalarVariable>
<!-- Index of variable = \"18\" -->
<ScalarVariable
name=\"SteamValve.dp\"
valueReference=\"128\"
description=\"Pressure difference between port_a and port_b (= port_a.p - port_b.p)\"
>
<Real unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"19\" -->
<ScalarVariable
name=\"SteamValve.port_a_T\"
valueReference=\"129\"
description=\"Temperature close to port_a, if show_T = true\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"20\" -->
<ScalarVariable
name=\"SteamValve.port_b_T\"
valueReference=\"130\"
description=\"Temperature close to port_b, if show_T = true\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"21\" -->
<ScalarVariable
name=\"T_S\"
valueReference=\"135\"
description=\"steam temperature\"
causality=\"output\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"22\" -->
<ScalarVariable
name=\"V_l\"
valueReference=\"136\"
description=\"liquid volume inside drum\"
causality=\"output\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"23\" -->
<ScalarVariable
name=\"Y_Valve\"
valueReference=\"137\"
description=\"valve opening\"
causality=\"input\"
>
<Real start=\"0.0\"/>
</ScalarVariable>
<!-- Index of variable = \"24\" -->
<ScalarVariable
name=\"controller.u\"
valueReference=\"138\"
description=\"Connector of Real input signal\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"25\" -->
<ScalarVariable
name=\"controller.y\"
valueReference=\"139\"
description=\"Connector of Real output signal\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"26\" -->
<ScalarVariable
name=\"evaporator.T_D\"
valueReference=\"140\"
description=\"temperature of drum\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"27\" -->
<ScalarVariable
name=\"evaporator.U\"
valueReference=\"141\"
description=\"internal energy\"
>
<Real unit=\"J\"/>
</ScalarVariable>
<!-- Index of variable = \"28\" -->
<ScalarVariable
name=\"evaporator.V_v\"
valueReference=\"142\"
description=\"volume of vapour phase\"
>
<Real unit=\"m3\"/>
</ScalarVariable>
<!-- Index of variable = \"29\" -->
<ScalarVariable
name=\"evaporator.h_S\"
valueReference=\"143\"
description=\"steam enthalpy (specific enthalpy close to steam port when mass flows in to the boiler)\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"30\" -->
<ScalarVariable
name=\"evaporator.h_l\"
valueReference=\"144\"
description=\"specific enthalpy of liquid\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"31\" -->
<ScalarVariable
name=\"evaporator.h_v\"
valueReference=\"145\"
description=\"specific enthalpy of vapour\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"32\" -->
<ScalarVariable
name=\"evaporator.m\"
valueReference=\"146\"
description=\"total mass of drum boiler\"
>
<Real min=\"0.0\" unit=\"kg\"/>
</ScalarVariable>
<!-- Index of variable = \"33\" -->
<ScalarVariable
name=\"evaporator.q_F\"
valueReference=\"147\"
description=\"heat flow rate from furnace\"
>
<Real unit=\"W\"/>
</ScalarVariable>
<!-- Index of variable = \"34\" -->
<ScalarVariable
name=\"evaporator.rho_l\"
valueReference=\"148\"
description=\"density in liquid phase\"
>
<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"35\" -->
<ScalarVariable
name=\"evaporator.rho_v\"
valueReference=\"149\"
description=\"density in vapour phase\"
>
<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"36\" -->
<ScalarVariable
name=\"limiter.y\"
valueReference=\"150\"
description=\"Connector of Real output signal\"
>
<Real min=\"-1e60\" max=\"1e5\"/>
</ScalarVariable>
<!-- Index of variable = \"37\" -->
<ScalarVariable
name=\"p_S\"
valueReference=\"151\"
description=\"steam pressure\"
causality=\"output\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"38\" -->
<ScalarVariable
name=\"pressure.port.h_outflow\"
valueReference=\"152\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
initial=\"exact\">
<Real start=\"1e5\" min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"39\" -->
<ScalarVariable
name=\"pressure.port.m_flow\"
valueReference=\"153\"
description=\"Mass flow rate from the connection point into the component\"
initial=\"exact\">
<Real start=\"0.0\" min=\"0.0\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"40\" -->
<ScalarVariable
name=\"pump.medium.MM\"
valueReference=\"156\"
description=\"Molar mass (of mixture or single fluid)\"
initial=\"exact\">
<Real start=\"0.0\" min=\"0.001\" max=\"0.25\" nominal=\"0.032\" unit=\"kg/mol\"/>
</ScalarVariable>
<!-- Index of variable = \"41\" -->
<ScalarVariable
name=\"pump.medium.R\"
valueReference=\"157\"
description=\"Gas constant (of mixture if applicable)\"
initial=\"exact\">
<Real start=\"1000.0\" min=\"0.0\" max=\"1e7\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
</ScalarVariable>
<!-- Index of variable = \"42\" -->
<ScalarVariable
name=\"pump.medium.T\"
valueReference=\"158\"
description=\"Temperature of medium\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"43\" -->
<ScalarVariable
name=\"pump.medium.T_degC\"
valueReference=\"159\"
description=\"Temperature of medium in [degC]\"
>
<Real unit=\"degC\"/>
</ScalarVariable>
<!-- Index of variable = \"44\" -->
<ScalarVariable
name=\"pump.medium.X[1]\"
valueReference=\"160\"
description=\"Mass fractions (= (component mass)/total mass m_i/m)\"
initial=\"exact\">
<Real start=\"1.0\" min=\"0.0\" max=\"1.0\" nominal=\"0.1\" unit=\"kg/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"45\" -->
<ScalarVariable
name=\"pump.medium.d\"
valueReference=\"161\"
description=\"Density of medium\"
>
<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"46\" -->
<ScalarVariable
name=\"pump.medium.p_bar\"
valueReference=\"162\"
description=\"Absolute pressure of medium in [bar]\"
>
<Real unit=\"bar\"/>
</ScalarVariable>
<!-- Index of variable = \"47\" -->
<ScalarVariable
name=\"pump.medium.sat.Tsat\"
valueReference=\"163\"
description=\"Saturation temperature\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"48\" -->
<ScalarVariable
name=\"pump.medium.u\"
valueReference=\"164\"
description=\"Specific internal energy of medium\"
>
<Real min=\"-1e8\" max=\"1e8\" nominal=\"1e6\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"49\" -->
<ScalarVariable
name=\"q_F\"
valueReference=\"165\"
description=\"fuel flow rate\"
causality=\"input\"
>
<Real start=\"0.0\" unit=\"MW\"/>
</ScalarVariable>
<!-- Index of variable = \"50\" -->
<ScalarVariable
name=\"qm_S\"
valueReference=\"166\"
description=\"steam flow rate\"
causality=\"output\"
>
<Real min=\"-1e60\" max=\"1e5\"/>
</ScalarVariable>
<!-- Index of variable = \"51\" -->
<ScalarVariable
name=\"sigma_D\"
valueReference=\"167\"
causality=\"output\"
>
<Real unit=\"N/mm2\"/>
</ScalarVariable>
<!-- Index of variable = \"52\" -->
<ScalarVariable
name=\"sink.medium.MM\"
valueReference=\"168\"
description=\"Molar mass (of mixture or single fluid)\"
initial=\"exact\">
<Real start=\"0.0\" min=\"0.001\" max=\"0.25\" nominal=\"0.032\" unit=\"kg/mol\"/>
</ScalarVariable>
<!-- Index of variable = \"53\" -->
<ScalarVariable
name=\"sink.medium.R\"
valueReference=\"169\"
description=\"Gas constant (of mixture if applicable)\"
initial=\"exact\">
<Real start=\"1000.0\" min=\"0.0\" max=\"1e7\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
</ScalarVariable>
<!-- Index of variable = \"54\" -->
<ScalarVariable
name=\"sink.medium.T_degC\"
valueReference=\"170\"
description=\"Temperature of medium in [degC]\"
>
<Real unit=\"degC\"/>
</ScalarVariable>
<!-- Index of variable = \"55\" -->
<ScalarVariable
name=\"sink.medium.X[1]\"
valueReference=\"171\"
description=\"Mass fractions (= (component mass)/total mass m_i/m)\"
initial=\"exact\">
<Real start=\"1.0\" min=\"0.0\" max=\"1.0\" nominal=\"0.1\" unit=\"kg/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"56\" -->
<ScalarVariable
name=\"sink.medium.d\"
valueReference=\"172\"
description=\"Density of medium\"
>
<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"57\" -->
<ScalarVariable
name=\"sink.medium.p_bar\"
valueReference=\"173\"
description=\"Absolute pressure of medium in [bar]\"
>
<Real unit=\"bar\"/>
</ScalarVariable>
<!-- Index of variable = \"58\" -->
<ScalarVariable
name=\"sink.medium.sat.Tsat\"
valueReference=\"174\"
description=\"Saturation temperature\"
initial=\"exact\">
<Real start=\"500.0\" min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"59\" -->
<ScalarVariable
name=\"sink.medium.u\"
valueReference=\"175\"
description=\"Specific internal energy of medium\"
>
<Real min=\"-1e8\" max=\"1e8\" nominal=\"1e6\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"60\" -->
<ScalarVariable
name=\"temperature.port.h_outflow\"
valueReference=\"178\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
initial=\"exact\">
<Real start=\"1e5\" min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"61\" -->
<ScalarVariable
name=\"temperature.port.m_flow\"
valueReference=\"179\"
description=\"Mass flow rate from the connection point into the component\"
initial=\"exact\">
<Real start=\"0.0\" min=\"0.0\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"62\" -->
<ScalarVariable
name=\"MW2W.k\"
valueReference=\"222\"
description=\"Gain value multiplied with input signal\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"1e6\" unit=\"1\"/>
</ScalarVariable>
<!-- Index of variable = \"63\" -->
<ScalarVariable
name=\"Pa2bar.k\"
valueReference=\"223\"
description=\"Gain value multiplied with input signal\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"1e-5\" unit=\"1\"/>
</ScalarVariable>
<!-- Index of variable = \"64\" -->
<ScalarVariable
name=\"SteamValve.dp_nominal\"
valueReference=\"224\"
description=\"Nominal pressure drop at full opening\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"9e6\" min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"65\" -->
<ScalarVariable
name=\"SteamValve.dp_start\"
valueReference=\"225\"
description=\"Guess value of dp = port_a.p - port_b.p\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"-1e60\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"66\" -->
<ScalarVariable
name=\"SteamValve.k\"
valueReference=\"226\"
description=\"Hydraulic conductance at full opening\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real unit=\"kg/(s.Pa)\"/>
</ScalarVariable>
<!-- Index of variable = \"67\" -->
<ScalarVariable
name=\"SteamValve.m_flow_nominal\"
valueReference=\"227\"
description=\"Nominal mass flowrate at full opening\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"180.0\" min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"68\" -->
<ScalarVariable
name=\"SteamValve.m_flow_small\"
valueReference=\"228\"
description=\"Small mass flow rate for regularization of zero flow\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"69\" -->
<ScalarVariable
name=\"SteamValve.m_flow_start\"
valueReference=\"229\"
description=\"Guess value of m_flow = port_a.m_flow\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"70\" -->
<ScalarVariable
name=\"SteamValve.port_b.p\"
valueReference=\"230\"
description=\"Thermodynamic pressure in the connection point\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"71\" -->
<ScalarVariable
name=\"controller.T\"
valueReference=\"232\"
description=\"Time Constant (T>0 required)\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"120.0\" min=\"1e-60\" unit=\"s\"/>
</ScalarVariable>
<!-- Index of variable = \"72\" -->
<ScalarVariable
name=\"controller.k\"
valueReference=\"233\"
description=\"Gain\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"10.0\" unit=\"1\"/>
</ScalarVariable>
<!-- Index of variable = \"73\" -->
<ScalarVariable
name=\"controller.x_start\"
valueReference=\"234\"
description=\"Initial or guess value of state\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"0.0\"/>
</ScalarVariable>
<!-- Index of variable = \"74\" -->
<ScalarVariable
name=\"controller.y_start\"
valueReference=\"235\"
description=\"Initial value of output\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"0.0\"/>
</ScalarVariable>
<!-- Index of variable = \"75\" -->
<ScalarVariable
name=\"evaporator.V_l_start\"
valueReference=\"236\"
description=\"Start value of liquid volumeStart value of volume\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"67.0\" unit=\"m3\"/>
</ScalarVariable>
<!-- Index of variable = \"76\" -->
<ScalarVariable
name=\"evaporator.V_t\"
valueReference=\"237\"
description=\"total volume inside drum\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"100.0\" unit=\"m3\"/>
</ScalarVariable>
<!-- Index of variable = \"77\" -->
<ScalarVariable
name=\"evaporator.cp_D\"
valueReference=\"238\"
description=\"specific heat capacity of drum metal\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"500.0\" min=\"0.0\" max=\"1e7\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
</ScalarVariable>
<!-- Index of variable = \"78\" -->
<ScalarVariable
name=\"evaporator.m_D\"
valueReference=\"239\"
description=\"mass of surrounding drum metal\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"3e5\" min=\"0.0\" unit=\"kg\"/>
</ScalarVariable>
<!-- Index of variable = \"79\" -->
<ScalarVariable
name=\"evaporator.p_start\"
valueReference=\"240\"
description=\"Start value of pressure\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"1e5\" min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"80\" -->
<ScalarVariable
name=\"feedback.u1\"
valueReference=\"241\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"81\" -->
<ScalarVariable
name=\"furnace.T_ref\"
valueReference=\"242\"
description=\"Reference temperature\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"293.15\" min=\"0.0\" nominal=\"300.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"82\" -->
<ScalarVariable
name=\"furnace.alpha\"
valueReference=\"243\"
description=\"Temperature coefficient of heat flow rate\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"0.0\" unit=\"1/K\"/>
</ScalarVariable>
<!-- Index of variable = \"83\" -->
<ScalarVariable
name=\"levelSetPoint.k\"
valueReference=\"244\"
description=\"Constant output value\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"67.0\"/>
</ScalarVariable>
<!-- Index of variable = \"84\" -->
<ScalarVariable
name=\"levelSetPoint.y\"
valueReference=\"245\"
description=\"Connector of Real output signal\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"85\" -->
<ScalarVariable
name=\"limiter.uMax\"
valueReference=\"246\"
description=\"Upper limits of input signals\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"500.0\"/>
</ScalarVariable>
<!-- Index of variable = \"86\" -->
<ScalarVariable
name=\"limiter.uMin\"
valueReference=\"247\"
description=\"Lower limits of input signals\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"0.0\"/>
</ScalarVariable>
<!-- Index of variable = \"87\" -->
<ScalarVariable
name=\"massFlowRate.m_flow_nominal\"
valueReference=\"248\"
description=\"Nominal value of m_flow = port_a.m_flow\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"88\" -->
<ScalarVariable
name=\"massFlowRate.m_flow_small\"
valueReference=\"249\"
description=\"Regularization for bi-directional flow in the region |m_flow| < m_flow_small (m_flow_small > 0 required)\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"0.0\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"89\" -->
<ScalarVariable
name=\"pump.X[1]\"
valueReference=\"250\"
description=\"Fixed value of composition\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"0.0\" max=\"1.0\" nominal=\"0.1\" unit=\"kg/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"90\" -->
<ScalarVariable
name=\"pump.h\"
valueReference=\"251\"
description=\"Fixed value of specific enthalpy\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"91\" -->
<ScalarVariable
name=\"pump.m_flow\"
valueReference=\"252\"
description=\"Fixed mass flow rate going out of the fluid port\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"92\" -->
<ScalarVariable
name=\"sink.T\"
valueReference=\"253\"
description=\"Boundary temperature\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"500.0\" min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"93\" -->
<ScalarVariable
name=\"sink.X[1]\"
valueReference=\"254\"
description=\"Boundary mass fractions m_i/m\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"1.0\" min=\"0.0\" max=\"1.0\" nominal=\"0.1\" unit=\"kg/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"94\" -->
<ScalarVariable
name=\"sink.d\"
valueReference=\"255\"
description=\"Boundary density\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"95\" -->
<ScalarVariable
name=\"sink.h\"
valueReference=\"256\"
description=\"Boundary specific enthalpy\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"84013.05815259689\" min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"96\" -->
<ScalarVariable
name=\"sink.medium.T\"
valueReference=\"257\"
description=\"Temperature of medium\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"97\" -->
<ScalarVariable
name=\"sink.medium.p\"
valueReference=\"258\"
description=\"Absolute pressure of medium\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"98\" -->
<ScalarVariable
name=\"sink.medium.sat.psat\"
valueReference=\"259\"
description=\"Saturation pressure\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"99\" -->
<ScalarVariable
name=\"sink.medium.state.T\"
valueReference=\"260\"
description=\"Temperature\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"100\" -->
<ScalarVariable
name=\"sink.medium.state.p\"
valueReference=\"261\"
description=\"Pressure\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"101\" -->
<ScalarVariable
name=\"sink.p\"
valueReference=\"262\"
description=\"Boundary pressure\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"5e4\" min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"102\" -->
<ScalarVariable
name=\"sink.ports[1].p\"
valueReference=\"263\"
description=\"Thermodynamic pressure in the connection point\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"103\" -->
<ScalarVariable
name=\"system.T_ambient\"
valueReference=\"266\"
description=\"Default ambient temperature\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"293.15\" min=\"0.0\" nominal=\"300.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"104\" -->
<ScalarVariable
name=\"system.T_start\"
valueReference=\"267\"
description=\"Default start value for temperatures\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"0.0\" nominal=\"300.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"105\" -->
<ScalarVariable
name=\"system.dp_small\"
valueReference=\"268\"
description=\"Default small pressure drop for regularization of laminar and zero flow\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"1.0\" min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"106\" -->
<ScalarVariable
name=\"system.eps_m_flow\"
valueReference=\"269\"
description=\"Regularization of zero flow for |m_flow| < eps_m_flow*m_flow_nominal\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"1e-4\" min=\"0.0\"/>
</ScalarVariable>
<!-- Index of variable = \"107\" -->
<ScalarVariable
name=\"system.g\"
valueReference=\"270\"
description=\"Constant gravity acceleration\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"9.80665\" unit=\"m/s2\"/>
</ScalarVariable>
<!-- Index of variable = \"108\" -->
<ScalarVariable
name=\"system.m_flow_nominal\"
valueReference=\"271\"
description=\"Default nominal mass flow rate\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"109\" -->
<ScalarVariable
name=\"system.m_flow_small\"
valueReference=\"272\"
description=\"Default small mass flow rate for regularization of laminar and zero flow\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"0.01\" min=\"0.0\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"110\" -->
<ScalarVariable
name=\"system.m_flow_start\"
valueReference=\"273\"
description=\"Default start value for mass flow rates\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"0.0\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"111\" -->
<ScalarVariable
name=\"system.p_ambient\"
valueReference=\"274\"
description=\"Default ambient pressure\"
variability=\"fixed\"
causality=\"parameter\"
>
<Real start=\"101325.0\" min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"112\" -->
<ScalarVariable
name=\"system.p_start\"
valueReference=\"275\"
description=\"Default start value for pressures\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Real min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"113\" -->
<ScalarVariable
name=\"K2degC.Celsius\"
valueReference=\"135\"
>
<Real unit=\"degC\"/>
</ScalarVariable>
<!-- Index of variable = \"114\" -->
<ScalarVariable
name=\"MW2W.u\"
valueReference=\"165\"
description=\"Input signal connector\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"115\" -->
<ScalarVariable
name=\"Pa2bar.u\"
valueReference=\"2\"
description=\"Input signal connector\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"116\" -->
<ScalarVariable
name=\"Pa2bar.y\"
valueReference=\"151\"
description=\"Output signal connector\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"117\" -->
<ScalarVariable
name=\"SteamValve.m_flow\"
valueReference=\"166\"
description=\"Mass flow rate in design flow direction\"
>
<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"118\" -->
<ScalarVariable
name=\"SteamValve.opening\"
valueReference=\"137\"
description=\"=1: completely open, =0: completely closed\"
>
<Real min=\"0.0\" max=\"1.0\"/>
</ScalarVariable>
<!-- Index of variable = \"119\" -->
<ScalarVariable
name=\"SteamValve.port_a.h_outflow\"
valueReference=\"143\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"120\" -->
<ScalarVariable
name=\"SteamValve.port_a.m_flow\"
valueReference=\"166\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"121\" -->
<ScalarVariable
name=\"SteamValve.port_a.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"122\" -->
<ScalarVariable
name=\"SteamValve.port_b.h_outflow\"
valueReference=\"145\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"123\" -->
<ScalarVariable
name=\"SteamValve.port_b.m_flow\"
valueReference=\"291\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real min=\"-1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"124\" -->
<ScalarVariable
name=\"evaporator.T\"
valueReference=\"140\"
description=\"temperature inside drum boiler\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"125\" -->
<ScalarVariable
name=\"evaporator.V\"
valueReference=\"1\"
description=\"liquid volume\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"126\" -->
<ScalarVariable
name=\"evaporator.h_W\"
valueReference=\"155\"
description=\"Feed water enthalpy (specific enthalpy close to feedwater port when mass flows in to the boiler)\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"127\" -->
<ScalarVariable
name=\"evaporator.heatPort.Q_flow\"
valueReference=\"147\"
description=\"Heat flow rate (positive if flowing from outside into the component)\"
>
<Real unit=\"W\"/>
</ScalarVariable>
<!-- Index of variable = \"128\" -->
<ScalarVariable
name=\"evaporator.heatPort.T\"
valueReference=\"140\"
description=\"Port temperature\"
>
<Real min=\"0.0\" nominal=\"300.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"129\" -->
<ScalarVariable
name=\"evaporator.port_a.h_outflow\"
valueReference=\"144\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"130\" -->
<ScalarVariable
name=\"evaporator.port_a.m_flow\"
valueReference=\"150\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"131\" -->
<ScalarVariable
name=\"evaporator.port_a.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"132\" -->
<ScalarVariable
name=\"evaporator.port_b.h_outflow\"
valueReference=\"145\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"133\" -->
<ScalarVariable
name=\"evaporator.port_b.m_flow\"
valueReference=\"304\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real min=\"-1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"134\" -->
<ScalarVariable
name=\"evaporator.port_b.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"135\" -->
<ScalarVariable
name=\"evaporator.qm_S\"
valueReference=\"306\"
description=\"steam mass flow rate\"
>
<Real min=\"-1e5\" max=\"1e60\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"136\" -->
<ScalarVariable
name=\"evaporator.qm_W\"
valueReference=\"150\"
description=\"feed water mass flow rate\"
>
<Real unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"137\" -->
<ScalarVariable
name=\"evaporator.sat.Tsat\"
valueReference=\"140\"
description=\"Saturation temperature\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"138\" -->
<ScalarVariable
name=\"evaporator.sat.psat\"
valueReference=\"2\"
description=\"Saturation pressure\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"139\" -->
<ScalarVariable
name=\"feedback.u2\"
valueReference=\"1\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"140\" -->
<ScalarVariable
name=\"feedback.y\"
valueReference=\"138\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"141\" -->
<ScalarVariable
name=\"furnace.Q_flow\"
valueReference=\"126\"
>
<Real unit=\"W\"/>
</ScalarVariable>
<!-- Index of variable = \"142\" -->
<ScalarVariable
name=\"furnace.port.Q_flow\"
valueReference=\"313\"
description=\"Heat flow rate (positive if flowing from outside into the component)\"
>
<Real unit=\"W\"/>
</ScalarVariable>
<!-- Index of variable = \"143\" -->
<ScalarVariable
name=\"furnace.port.T\"
valueReference=\"140\"
description=\"Port temperature\"
>
<Real min=\"0.0\" nominal=\"300.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"144\" -->
<ScalarVariable
name=\"limiter.u\"
valueReference=\"139\"
description=\"Connector of Real input signal\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"145\" -->
<ScalarVariable
name=\"massFlowRate.m_flow\"
valueReference=\"166\"
description=\"Mass flow rate from port_a to port_b\"
>
<Real unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"146\" -->
<ScalarVariable
name=\"massFlowRate.port_a.h_outflow\"
valueReference=\"143\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"147\" -->
<ScalarVariable
name=\"massFlowRate.port_a.m_flow\"
valueReference=\"166\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"148\" -->
<ScalarVariable
name=\"massFlowRate.port_a.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"149\" -->
<ScalarVariable
name=\"massFlowRate.port_b.h_outflow\"
valueReference=\"145\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"150\" -->
<ScalarVariable
name=\"massFlowRate.port_b.m_flow\"
valueReference=\"321\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real min=\"-1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"151\" -->
<ScalarVariable
name=\"massFlowRate.port_b.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"152\" -->
<ScalarVariable
name=\"pressure.p\"
valueReference=\"2\"
description=\"Pressure at port\"
>
<Real min=\"0.0\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"153\" -->
<ScalarVariable
name=\"pressure.port.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"154\" -->
<ScalarVariable
name=\"pump.m_flow_in\"
valueReference=\"150\"
description=\"Prescribed mass flow rate\"
>
<Real/>
</ScalarVariable>
<!-- Index of variable = \"155\" -->
<ScalarVariable
name=\"pump.medium.h\"
valueReference=\"155\"
description=\"Specific enthalpy of medium\"
>
<Real unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"156\" -->
<ScalarVariable
name=\"pump.medium.p\"
valueReference=\"2\"
description=\"Absolute pressure of medium\"
>
<Real min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"157\" -->
<ScalarVariable
name=\"pump.medium.sat.psat\"
valueReference=\"2\"
description=\"Saturation pressure\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"158\" -->
<ScalarVariable
name=\"pump.medium.state.T\"
valueReference=\"158\"
description=\"Temperature\"
>
<Real min=\"273.15\" max=\"2273.15\" nominal=\"500.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"159\" -->
<ScalarVariable
name=\"pump.medium.state.d\"
valueReference=\"161\"
description=\"Density\"
>
<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"160\" -->
<ScalarVariable
name=\"pump.medium.state.h\"
valueReference=\"155\"
description=\"Specific enthalpy\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"161\" -->
<ScalarVariable
name=\"pump.medium.state.p\"
valueReference=\"2\"
description=\"Pressure\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"162\" -->
<ScalarVariable
name=\"pump.ports[1].h_outflow\"
valueReference=\"155\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"163\" -->
<ScalarVariable
name=\"pump.ports[1].m_flow\"
valueReference=\"335\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"164\" -->
<ScalarVariable
name=\"pump.ports[1].p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"165\" -->
<ScalarVariable
name=\"sink.medium.h\"
valueReference=\"143\"
description=\"Specific enthalpy of medium\"
>
<Real unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"166\" -->
<ScalarVariable
name=\"sink.medium.state.d\"
valueReference=\"172\"
description=\"Density\"
>
<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"167\" -->
<ScalarVariable
name=\"sink.medium.state.h\"
valueReference=\"143\"
description=\"Specific enthalpy\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"168\" -->
<ScalarVariable
name=\"sink.ports[1].h_outflow\"
valueReference=\"143\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"169\" -->
<ScalarVariable
name=\"sink.ports[1].m_flow\"
valueReference=\"166\"
description=\"Mass flow rate from the connection point into the component\"
>
<Real unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"170\" -->
<ScalarVariable
name=\"temperature.T\"
valueReference=\"125\"
description=\"Temperature in port medium\"
>
<Real min=\"0.0\" unit=\"K\"/>
</ScalarVariable>
<!-- Index of variable = \"171\" -->
<ScalarVariable
name=\"temperature.port.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"172\" -->
<ScalarVariable
name=\"pump.medium.phase\"
valueReference=\"14\"
description=\"2 for two-phase, 1 for one-phase, 0 if not known\"
variability=\"discrete\"
>
<Integer/>
</ScalarVariable>
<!-- Index of variable = \"173\" -->
<ScalarVariable
name=\"sink.medium.phase\"
valueReference=\"15\"
description=\"2 for two-phase, 1 for one-phase, 0 if not known\"
variability=\"discrete\"
initial=\"exact\">
<Integer start=\"1\"/>
</ScalarVariable>
<!-- Index of variable = \"174\" -->
<ScalarVariable
name=\"controller.initType\"
valueReference=\"23\"
description=\"Type of initialization (1: no init, 2: steady state, 3: initial state, 4: initial output)\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
<Enumeration declaredTyp
...[truncated 19327 chars]...
ELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_02nls.o DrumBoilerModel_me_FMU_02nls.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_03lsy.o DrumBoilerModel_me_FMU_03lsy.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_04set.o DrumBoilerModel_me_FMU_04set.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_05evt.o DrumBoilerModel_me_FMU_05evt.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_06inz.o DrumBoilerModel_me_FMU_06inz.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_07dly.o DrumBoilerModel_me_FMU_07dly.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_08bnd.o DrumBoilerModel_me_FMU_08bnd.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_09alg.o DrumBoilerModel_me_FMU_09alg.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_10asr.o DrumBoilerModel_me_FMU_10asr.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_11mix.o DrumBoilerModel_me_FMU_11mix.c
clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_12jac.o DrumBoilerModel_me_FMU_12jac.c
DrumBoilerModel_me_FMU_12jac.c:196:50: error: use of undeclared identifier '_omcQ_24TMP_5F424'
real_array_create(&tmp15, ((modelica_real*)&((&_omcQ_24TMP_5F424)[((modelica_integer) 1) - 1])), 1, (_index_t)3);
^
DrumBoilerModel_me_FMU_12jac.c:212:94: error: use of undeclared identifier '_omcQ_24TMP_5F424'
jacobian->resultVars[0] /* der(fmi_x.$pDERA.dummyVarA[1]) JACOBIAN_VAR */ = real_array_get(_omcQ_24TMP_5F424, 1, ((modelica_integer) 1));
^
DrumBoilerModel_me_FMU_12jac.c:227:94: error: use of undeclared identifier '_omcQ_24TMP_5F424'
jacobian->resultVars[1] /* der(fmi_x.$pDERA.dummyVarA[2]) JACOBIAN_VAR */ = real_array_get(_omcQ_24TMP_5F424, 1, ((modelica_integer) 2));
^
DrumBoilerModel_me_FMU_12jac.c:242:94: error: use of undeclared identifier '_omcQ_24TMP_5F424'
jacobian->resultVars[2] /* der(fmi_x.$pDERA.dummyVarA[3]) JACOBIAN_VAR */ = real_array_get(_omcQ_24TMP_5F424, 1, ((modelica_integer) 3));
^
4 errors generated.
make: *** [<builtin>: DrumBoilerModel_me_FMU_12jac.o] Error 1
"
Equation mismatch: diff says:
--- /tmp/omc-rtest-unknown/openmodelica/cppruntime/fmu/modelExchange/2.0/testDrumBoiler.mos_temp5065/equations-expected2024-01-20 03:55:56.438552277 +0000
+++ /tmp/omc-rtest-unknown/openmodelica/cppruntime/fmu/modelExchange/2.0/testDrumBoiler.mos_temp5065/equations-got2024-01-20 03:56:48.682205141 +0000
@@ -35,17 +35,17 @@
</Unit>
<Unit name=\"1\">
<BaseUnit />
</Unit>
<Unit name=\"N/mm2\">
-<BaseUnit m=\"-1\" s=\"-2\" kg=\"1\" factor=\"1000000.0\" />
+<BaseUnit m=\"-1\" s=\"-2\" kg=\"1\" factor=\"1e6\" />
</Unit>
<Unit name=\"MW\">
-<BaseUnit m=\"2\" s=\"-3\" kg=\"1\" factor=\"1000000.0\" />
+<BaseUnit m=\"2\" s=\"-3\" kg=\"1\" factor=\"1e6\" />
</Unit>
<Unit name=\"bar\">
-<BaseUnit m=\"-1\" s=\"-2\" kg=\"1\" factor=\"100000.0\" />
+<BaseUnit m=\"-1\" s=\"-2\" kg=\"1\" factor=\"1e5\" />
</Unit>
<Unit name=\"kg/kg\">
<BaseUnit />
</Unit>
<Unit name=\"degC\">
@@ -80,11 +80,11 @@
</Unit>
<Unit name=\"K\">
<BaseUnit K=\"1\" />
</Unit>
<Unit name=\"km-1.s-3.g\">
-<BaseUnit m=\"-1\" s=\"-3\" kg=\"1\" factor=\"1e-06\" />
+<BaseUnit m=\"-1\" s=\"-3\" kg=\"1\" factor=\"1e-6\" />
</Unit>
<Unit name=\"m3.s-1\">
<BaseUnit m=\"3\" s=\"-1\" />
</Unit>
<Unit name=\"Pa\">
@@ -130,11 +130,11 @@
<Category name=\"logStatusFatal\" />
<Category name=\"logStatusPending\" />
<Category name=\"logAll\" />
<Category name=\"logFmi2Call\" />
</LogCategories>
-<DefaultExperiment startTime=\"0.0\" stopTime=\"1.0\" tolerance=\"1e-06\"/>
+<DefaultExperiment startTime=\"0.0\" stopTime=\"1.0\" tolerance=\"1e-6\"/>
<ModelVariables>
<!-- Index of variable = \"1\" -->
<ScalarVariable
name=\"controller.x\"
valueReference=\"0\"
@@ -154,11 +154,11 @@
<ScalarVariable
name=\"evaporator.p\"
valueReference=\"2\"
description=\"pressure inside drum boiler\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"4\" -->
<ScalarVariable
name=\"der(controller.x)\"
valueReference=\"3\"
@@ -178,11 +178,11 @@
<ScalarVariable
name=\"der(evaporator.p)\"
valueReference=\"5\"
description=\"der(pressure inside drum boiler)\"
initial=\"approx\">
-<Real start=\"0.0\" derivative=\"3\" nominal=\"500000000.0\" unit=\"km-1.s-3.g\"/>
+<Real start=\"0.0\" derivative=\"3\" nominal=\"5e8\" unit=\"km-1.s-3.g\"/>
</ScalarVariable>
<!-- Index of variable = \"7\" -->
<ScalarVariable
name=\"der(evaporator.T_D)\"
valueReference=\"6\"
@@ -364,27 +364,27 @@
<ScalarVariable
name=\"evaporator.h_S\"
valueReference=\"143\"
description=\"steam enthalpy (specific enthalpy close to steam port when mass flows in to the boiler)\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"30\" -->
<ScalarVariable
name=\"evaporator.h_l\"
valueReference=\"144\"
description=\"specific enthalpy of liquid\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"31\" -->
<ScalarVariable
name=\"evaporator.h_v\"
valueReference=\"145\"
description=\"specific enthalpy of vapour\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"32\" -->
<ScalarVariable
name=\"evaporator.m\"
valueReference=\"146\"
@@ -404,27 +404,27 @@
<ScalarVariable
name=\"evaporator.rho_l\"
valueReference=\"148\"
description=\"density in liquid phase\"
>
-<Real min=\"0.0\" max=\"100000.0\" nominal=\"500.0\" unit=\"kg/m3\"/>
+<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"35\" -->
<ScalarVariable
name=\"evaporator.rho_v\"
valueReference=\"149\"
description=\"density in vapour phase\"
>
-<Real min=\"0.0\" max=\"100000.0\" nominal=\"500.0\" unit=\"kg/m3\"/>
+<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"36\" -->
<ScalarVariable
name=\"limiter.y\"
valueReference=\"150\"
description=\"Connector of Real output signal\"
>
-<Real min=\"-9.999999999999999e+59\" max=\"100000.0\"/>
+<Real min=\"-1e60\" max=\"1e5\"/>
</ScalarVariable>
<!-- Index of variable = \"37\" -->
<ScalarVariable
name=\"p_S\"
valueReference=\"151\"
@@ -437,19 +437,19 @@
<ScalarVariable
name=\"pressure.port.h_outflow\"
valueReference=\"152\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
initial=\"exact\">
-<Real start=\"100000.0\" min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real start=\"1e5\" min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"39\" -->
<ScalarVariable
name=\"pressure.port.m_flow\"
valueReference=\"153\"
description=\"Mass flow rate from the connection point into the component\"
initial=\"exact\">
-<Real start=\"0.0\" min=\"0.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real start=\"0.0\" min=\"0.0\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"40\" -->
<ScalarVariable
name=\"pump.medium.MM\"
valueReference=\"156\"
@@ -461,11 +461,11 @@
<ScalarVariable
name=\"pump.medium.R\"
valueReference=\"157\"
description=\"Gas constant (of mixture if applicable)\"
initial=\"exact\">
-<Real start=\"1000.0\" min=\"0.0\" max=\"10000000.0\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
+<Real start=\"1000.0\" min=\"0.0\" max=\"1e7\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
</ScalarVariable>
<!-- Index of variable = \"42\" -->
<ScalarVariable
name=\"pump.medium.T\"
valueReference=\"158\"
@@ -493,11 +493,11 @@
<ScalarVariable
name=\"pump.medium.d\"
valueReference=\"161\"
description=\"Density of medium\"
>
-<Real min=\"0.0\" max=\"100000.0\" nominal=\"500.0\" unit=\"kg/m3\"/>
+<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"46\" -->
<ScalarVariable
name=\"pump.medium.p_bar\"
valueReference=\"162\"
@@ -517,11 +517,11 @@
<ScalarVariable
name=\"pump.medium.u\"
valueReference=\"164\"
description=\"Specific internal energy of medium\"
>
-<Real min=\"-100000000.0\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e8\" max=\"1e8\" nominal=\"1e6\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"49\" -->
<ScalarVariable
name=\"q_F\"
valueReference=\"165\"
@@ -535,11 +535,11 @@
name=\"qm_S\"
valueReference=\"166\"
description=\"steam flow rate\"
causality=\"output\"
>
-<Real min=\"-9.999999999999999e+59\" max=\"100000.0\"/>
+<Real min=\"-1e60\" max=\"1e5\"/>
</ScalarVariable>
<!-- Index of variable = \"51\" -->
<ScalarVariable
name=\"sigma_D\"
valueReference=\"167\"
@@ -559,11 +559,11 @@
<ScalarVariable
name=\"sink.medium.R\"
valueReference=\"169\"
description=\"Gas constant (of mixture if applicable)\"
initial=\"exact\">
-<Real start=\"1000.0\" min=\"0.0\" max=\"10000000.0\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
+<Real start=\"1000.0\" min=\"0.0\" max=\"1e7\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
</ScalarVariable>
<!-- Index of variable = \"54\" -->
<ScalarVariable
name=\"sink.medium.T_degC\"
valueReference=\"170\"
@@ -583,11 +583,11 @@
<ScalarVariable
name=\"sink.medium.d\"
valueReference=\"172\"
description=\"Density of medium\"
>
-<Real min=\"0.0\" max=\"100000.0\" nominal=\"500.0\" unit=\"kg/m3\"/>
+<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"57\" -->
<ScalarVariable
name=\"sink.medium.p_bar\"
valueReference=\"173\"
@@ -607,67 +607,67 @@
<ScalarVariable
name=\"sink.medium.u\"
valueReference=\"175\"
description=\"Specific internal energy of medium\"
>
-<Real min=\"-100000000.0\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e8\" max=\"1e8\" nominal=\"1e6\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"60\" -->
<ScalarVariable
name=\"temperature.port.h_outflow\"
valueReference=\"178\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
initial=\"exact\">
-<Real start=\"100000.0\" min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real start=\"1e5\" min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"61\" -->
<ScalarVariable
name=\"temperature.port.m_flow\"
valueReference=\"179\"
description=\"Mass flow rate from the connection point into the component\"
initial=\"exact\">
-<Real start=\"0.0\" min=\"0.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real start=\"0.0\" min=\"0.0\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"62\" -->
<ScalarVariable
name=\"MW2W.k\"
valueReference=\"222\"
description=\"Gain value multiplied with input signal\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"1000000.0\" unit=\"1\"/>
+<Real start=\"1e6\" unit=\"1\"/>
</ScalarVariable>
<!-- Index of variable = \"63\" -->
<ScalarVariable
name=\"Pa2bar.k\"
valueReference=\"223\"
description=\"Gain value multiplied with input signal\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"1e-05\" unit=\"1\"/>
+<Real start=\"1e-5\" unit=\"1\"/>
</ScalarVariable>
<!-- Index of variable = \"64\" -->
<ScalarVariable
name=\"SteamValve.dp_nominal\"
valueReference=\"224\"
description=\"Nominal pressure drop at full opening\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"9000000.0\" min=\"0.0\" nominal=\"100000.0\" unit=\"Pa\"/>
+<Real start=\"9e6\" min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"65\" -->
<ScalarVariable
name=\"SteamValve.dp_start\"
valueReference=\"225\"
description=\"Guess value of dp = port_a.p - port_b.p\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"-9.999999999999999e+59\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"-1e60\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"66\" -->
<ScalarVariable
name=\"SteamValve.k\"
valueReference=\"226\"
@@ -683,41 +683,41 @@
valueReference=\"227\"
description=\"Nominal mass flowrate at full opening\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"180.0\" min=\"-100000.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real start=\"180.0\" min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"68\" -->
<ScalarVariable
name=\"SteamValve.m_flow_small\"
valueReference=\"228\"
description=\"Small mass flow rate for regularization of zero flow\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"-100000.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"69\" -->
<ScalarVariable
name=\"SteamValve.m_flow_start\"
valueReference=\"229\"
description=\"Guess value of m_flow = port_a.m_flow\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"-100000.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"70\" -->
<ScalarVariable
name=\"SteamValve.port_b.p\"
valueReference=\"230\"
description=\"Thermodynamic pressure in the connection point\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"71\" -->
<ScalarVariable
name=\"controller.T\"
valueReference=\"232\"
@@ -783,31 +783,31 @@
valueReference=\"238\"
description=\"specific heat capacity of drum metal\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"500.0\" min=\"0.0\" max=\"10000000.0\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
+<Real start=\"500.0\" min=\"0.0\" max=\"1e7\" nominal=\"1000.0\" unit=\"J/(kg.K)\"/>
</ScalarVariable>
<!-- Index of variable = \"78\" -->
<ScalarVariable
name=\"evaporator.m_D\"
valueReference=\"239\"
description=\"mass of surrounding drum metal\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"300000.0\" min=\"0.0\" unit=\"kg\"/>
+<Real start=\"3e5\" min=\"0.0\" unit=\"kg\"/>
</ScalarVariable>
<!-- Index of variable = \"79\" -->
<ScalarVariable
name=\"evaporator.p_start\"
valueReference=\"240\"
description=\"Start value of pressure\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"100000.0\" min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real start=\"1e5\" min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"80\" -->
<ScalarVariable
name=\"feedback.u1\"
valueReference=\"241\"
@@ -882,21 +882,21 @@
valueReference=\"248\"
description=\"Nominal value of m_flow = port_a.m_flow\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"-100000.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"88\" -->
<ScalarVariable
name=\"massFlowRate.m_flow_small\"
valueReference=\"249\"
description=\"Regularization for bi-directional flow in the region |m_flow| < m_flow_small (m_flow_small > 0 required)\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"0.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real min=\"0.0\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"89\" -->
<ScalarVariable
name=\"pump.X[1]\"
valueReference=\"250\"
@@ -912,21 +912,21 @@
valueReference=\"251\"
description=\"Fixed value of specific enthalpy\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"91\" -->
<ScalarVariable
name=\"pump.m_flow\"
valueReference=\"252\"
description=\"Fixed mass flow rate going out of the fluid port\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"-100000.0\" max=\"100000.0\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"92\" -->
<ScalarVariable
name=\"sink.T\"
valueReference=\"253\"
@@ -952,21 +952,21 @@
valueReference=\"255\"
description=\"Boundary density\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"0.0\" max=\"100000.0\" nominal=\"500.0\" unit=\"kg/m3\"/>
+<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"95\" -->
<ScalarVariable
name=\"sink.h\"
valueReference=\"256\"
description=\"Boundary specific enthalpy\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"84013.05815259689\" min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real start=\"84013.05815259689\" min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"96\" -->
<ScalarVariable
name=\"sink.medium.T\"
valueReference=\"257\"
@@ -982,21 +982,21 @@
valueReference=\"258\"
description=\"Absolute pressure of medium\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"0.0\" nominal=\"100000.0\" unit=\"Pa\"/>
+<Real min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"98\" -->
<ScalarVariable
name=\"sink.medium.sat.psat\"
valueReference=\"259\"
description=\"Saturation pressure\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"99\" -->
<ScalarVariable
name=\"sink.medium.state.T\"
valueReference=\"260\"
@@ -1012,31 +1012,31 @@
valueReference=\"261\"
description=\"Pressure\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"101\" -->
<ScalarVariable
name=\"sink.p\"
valueReference=\"262\"
description=\"Boundary pressure\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"50000.0\" min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real start=\"5e4\" min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"102\" -->
<ScalarVariable
name=\"sink.ports[1].p\"
valueReference=\"263\"
description=\"Thermodynamic pressure in the connection point\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"103\" -->
<ScalarVariable
name=\"system.T_ambient\"
valueReference=\"266\"
@@ -1062,31 +1062,31 @@
valueReference=\"268\"
description=\"Default small pressure drop for regularization of laminar and zero flow\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"1.0\" min=\"0.0\" nominal=\"100000.0\" unit=\"Pa\"/>
+<Real start=\"1.0\" min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"106\" -->
<ScalarVariable
name=\"system.eps_m_flow\"
valueReference=\"269\"
description=\"Regularization of zero flow for |m_flow| < eps_m_flow*m_flow_nominal\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"0.0001\" min=\"0.0\"/>
+<Real start=\"1e-4\" min=\"0.0\"/>
</ScalarVariable>
<!-- Index of variable = \"107\" -->
<ScalarVariable
name=\"system.g\"
valueReference=\"270\"
description=\"Constant gravity acceleration\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"9.806649999999999\" unit=\"m/s2\"/>
+<Real start=\"9.80665\" unit=\"m/s2\"/>
</ScalarVariable>
<!-- Index of variable = \"108\" -->
<ScalarVariable
name=\"system.m_flow_nominal\"
valueReference=\"271\"
@@ -1122,21 +1122,21 @@
valueReference=\"274\"
description=\"Default ambient pressure\"
variability=\"fixed\"
causality=\"parameter\"
>
-<Real start=\"101325.0\" min=\"0.0\" nominal=\"100000.0\" unit=\"Pa\"/>
+<Real start=\"101325.0\" min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"112\" -->
<ScalarVariable
name=\"system.p_start\"
valueReference=\"275\"
description=\"Default start value for pressures\"
variability=\"fixed\"
causality=\"calculatedParameter\"
>
-<Real min=\"0.0\" nominal=\"100000.0\" unit=\"Pa\"/>
+<Real min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"113\" -->
<ScalarVariable
name=\"K2degC.Celsius\"
valueReference=\"135\"
@@ -1171,11 +1171,11 @@
<ScalarVariable
name=\"SteamValve.m_flow\"
valueReference=\"166\"
description=\"Mass flow rate in design flow direction\"
>
-<Real max=\"100000.0\" unit=\"kg/s\"/>
+<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"118\" -->
<ScalarVariable
name=\"SteamValve.opening\"
valueReference=\"137\"
@@ -1187,43 +1187,43 @@
<ScalarVariable
name=\"SteamValve.port_a.h_outflow\"
valueReference=\"143\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"120\" -->
<ScalarVariable
name=\"SteamValve.port_a.m_flow\"
valueReference=\"166\"
description=\"Mass flow rate from the connection point into the component\"
>
-<Real max=\"100000.0\" unit=\"kg/s\"/>
+<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"121\" -->
<ScalarVariable
name=\"SteamValve.port_a.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"122\" -->
<ScalarVariable
name=\"SteamValve.port_b.h_outflow\"
valueReference=\"145\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"123\" -->
<ScalarVariable
name=\"SteamValve.port_b.m_flow\"
valueReference=\"291\"
description=\"Mass flow rate from the connection point into the component\"
>
-<Real min=\"-100000.0\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"124\" -->
<ScalarVariable
name=\"evaporator.T\"
valueReference=\"140\"
@@ -1243,11 +1243,11 @@
<ScalarVariable
name=\"evaporator.h_W\"
valueReference=\"155\"
description=\"Feed water enthalpy (specific enthalpy close to feedwater port when mass flows in to the boiler)\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"127\" -->
<ScalarVariable
name=\"evaporator.heatPort.Q_flow\"
valueReference=\"147\"
@@ -1267,59 +1267,59 @@
<ScalarVariable
name=\"evaporator.port_a.h_outflow\"
valueReference=\"144\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"130\" -->
<ScalarVariable
name=\"evaporator.port_a.m_flow\"
valueReference=\"150\"
description=\"Mass flow rate from the connection point into the component\"
>
-<Real max=\"100000.0\" unit=\"kg/s\"/>
+<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"131\" -->
<ScalarVariable
name=\"evaporator.port_a.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"132\" -->
<ScalarVariable
name=\"evaporator.port_b.h_outflow\"
valueReference=\"145\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"133\" -->
<ScalarVariable
name=\"evaporator.port_b.m_flow\"
valueReference=\"304\"
description=\"Mass flow rate from the connection point into the component\"
>
-<Real min=\"-100000.0\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"134\" -->
<ScalarVariable
name=\"evaporator.port_b.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"135\" -->
<ScalarVariable
name=\"evaporator.qm_S\"
valueReference=\"306\"
description=\"steam mass flow rate\"
>
-<Real min=\"-100000.0\" max=\"9.999999999999999e+59\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" max=\"1e60\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"136\" -->
<ScalarVariable
name=\"evaporator.qm_W\"
valueReference=\"150\"
@@ -1339,11 +1339,11 @@
<ScalarVariable
name=\"evaporator.sat.psat\"
valueReference=\"2\"
description=\"Saturation pressure\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"139\" -->
<ScalarVariable
name=\"feedback.u2\"
valueReference=\"1\"
@@ -1400,51 +1400,51 @@
<ScalarVariable
name=\"massFlowRate.port_a.h_outflow\"
valueReference=\"143\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"147\" -->
<ScalarVariable
name=\"massFlowRate.port_a.m_flow\"
valueReference=\"166\"
description=\"Mass flow rate from the connection point into the component\"
>
-<Real max=\"100000.0\" unit=\"kg/s\"/>
+<Real max=\"1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"148\" -->
<ScalarVariable
name=\"massFlowRate.port_a.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"149\" -->
<ScalarVariable
name=\"massFlowRate.port_b.h_outflow\"
valueReference=\"145\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"150\" -->
<ScalarVariable
name=\"massFlowRate.port_b.m_flow\"
valueReference=\"321\"
description=\"Mass flow rate from the connection point into the component\"
>
-<Real min=\"-100000.0\" unit=\"kg/s\"/>
+<Real min=\"-1e5\" unit=\"kg/s\"/>
</ScalarVariable>
<!-- Index of variable = \"151\" -->
<ScalarVariable
name=\"massFlowRate.port_b.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"152\" -->
<ScalarVariable
name=\"pressure.p\"
valueReference=\"2\"
@@ -1456,11 +1456,11 @@
<ScalarVariable
name=\"pressure.port.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"154\" -->
<ScalarVariable
name=\"pump.m_flow_in\"
valueReference=\"150\"
@@ -1480,19 +1480,19 @@
<ScalarVariable
name=\"pump.medium.p\"
valueReference=\"2\"
description=\"Absolute pressure of medium\"
>
-<Real min=\"0.0\" nominal=\"100000.0\" unit=\"Pa\"/>
+<Real min=\"0.0\" nominal=\"1e5\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"157\" -->
<ScalarVariable
name=\"pump.medium.sat.psat\"
valueReference=\"2\"
description=\"Saturation pressure\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"158\" -->
<ScalarVariable
name=\"pump.medium.state.T\"
valueReference=\"158\"
@@ -1504,35 +1504,35 @@
<ScalarVariable
name=\"pump.medium.state.d\"
valueReference=\"161\"
description=\"Density\"
>
-<Real min=\"0.0\" max=\"100000.0\" nominal=\"500.0\" unit=\"kg/m3\"/>
+<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"160\" -->
<ScalarVariable
name=\"pump.medium.state.h\"
valueReference=\"155\"
description=\"Specific enthalpy\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"161\" -->
<ScalarVariable
name=\"pump.medium.state.p\"
valueReference=\"2\"
description=\"Pressure\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"162\" -->
<ScalarVariable
name=\"pump.ports[1].h_outflow\"
valueReference=\"155\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"163\" -->
<ScalarVariable
name=\"pump.ports[1].m_flow\"
valueReference=\"335\"
@@ -1544,11 +1544,11 @@
<ScalarVariable
name=\"pump.ports[1].p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"165\" -->
<ScalarVariable
name=\"sink.medium.h\"
valueReference=\"143\"
@@ -1560,27 +1560,27 @@
<ScalarVariable
name=\"sink.medium.state.d\"
valueReference=\"172\"
description=\"Density\"
>
-<Real min=\"0.0\" max=\"100000.0\" nominal=\"500.0\" unit=\"kg/m3\"/>
+<Real min=\"0.0\" max=\"1e5\" nominal=\"500.0\" unit=\"kg/m3\"/>
</ScalarVariable>
<!-- Index of variable = \"167\" -->
<ScalarVariable
name=\"sink.medium.state.h\"
valueReference=\"143\"
description=\"Specific enthalpy\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"168\" -->
<ScalarVariable
name=\"sink.ports[1].h_outflow\"
valueReference=\"143\"
description=\"Specific thermodynamic enthalpy close to the connection point if m_flow < 0\"
>
-<Real min=\"-10000000000.0\" max=\"10000000000.0\" nominal=\"500000.0\" unit=\"J/kg\"/>
+<Real min=\"-1e10\" max=\"1e10\" nominal=\"5e5\" unit=\"J/kg\"/>
</ScalarVariable>
<!-- Index of variable = \"169\" -->
<ScalarVariable
name=\"sink.ports[1].m_flow\"
valueReference=\"166\"
@@ -1600,11 +1600,11 @@
<ScalarVariable
name=\"temperature.port.p\"
valueReference=\"2\"
description=\"Thermodynamic pressure in the connection point\"
>
-<Real min=\"611.657\" max=\"100000000.0\" nominal=\"1000000.0\" unit=\"Pa\"/>
+<Real min=\"611.657\" max=\"1e8\" nominal=\"1e6\" unit=\"Pa\"/>
</ScalarVariable>
<!-- Index of variable = \"172\" -->
<ScalarVariable
name=\"pump.medium.phase\"
valueReference=\"14\"
@@ -2025,20 +2025,47 @@
true
""
true
""
record SimulationResult
-resultFile = "DrumBoilerModel_me_FMU_res.mat",
-simulationOptions = "startTime = 0.0, stopTime = 100.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'DrumBoilerModel_me_FMU', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-override=q_F=10,Y_Valve=1'",
-messages = "LOG_SUCCESS | info | The initialization finished successfully without homotopy method.
-LOG_SUCCESS | info | The simulation finished successfully.
-"
+resultFile = "",
+simulationOptions = "startTime = 0.0, stopTime = 100.0, numberOfIntervals = 500, tolerance = 1e-6, method = 'dassl', fileNamePrefix = 'DrumBoilerModel_me_FMU', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-override=q_F=10,Y_Valve=1'",
+messages = "Failed to build model: DrumBoilerModel_me_FMU"
end SimulationResult;
-""
-10.0
-1.0
-1.066186930067678
-1.132373860135355
--16.62186190266388
-101.410212034632
-66.98717532203514
--1.132373860135355
+"Error: Error building simulator. Build log: clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU.o DrumBoilerModel_me_FMU.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_functions.o DrumBoilerModel_me_FMU_functions.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_records.o DrumBoilerModel_me_FMU_records.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_01exo.o DrumBoilerModel_me_FMU_01exo.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_02nls.o DrumBoilerModel_me_FMU_02nls.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_03lsy.o DrumBoilerModel_me_FMU_03lsy.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_04set.o DrumBoilerModel_me_FMU_04set.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_05evt.o DrumBoilerModel_me_FMU_05evt.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_06inz.o DrumBoilerModel_me_FMU_06inz.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_07dly.o DrumBoilerModel_me_FMU_07dly.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_08bnd.o DrumBoilerModel_me_FMU_08bnd.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_09alg.o DrumBoilerModel_me_FMU_09alg.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_10asr.o DrumBoilerModel_me_FMU_10asr.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_11mix.o DrumBoilerModel_me_FMU_11mix.c
+clang -O0 -DOM_HAVE_PTHREADS -fPIC -falign-functions -mfpmath=sse -fno-dollars-in-identifiers -Wno-parentheses-equality -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc/c\" -I\"/var/lib/jenkins2/ws/OpenModelica_PR-9221/build/bin/../include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=DrumBoilerModel_me_FMU -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o DrumBoilerModel_me_FMU_12jac.o DrumBoilerModel_me_FMU_12jac.c
+DrumBoilerModel_me_FMU_12jac.c:196:50: error: use of undeclared identifier '_omcQ_24TMP_5F424'
+real_array_create(&tmp15, ((modelica_real*)&((&_omcQ_24TMP_5F424)[((modelica_integer) 1) - 1])), 1, (_index_t)3);
+^
+DrumBoilerModel_me_FMU_12jac.c:212:94: error: use of undeclared identifier '_omcQ_24TMP_5F424'
+jacobian->resultVars[0] /* der(fmi_x.$pDERA.dummyVarA[1]) JACOBIAN_VAR */ = real_array_get(_omcQ_24TMP_5F424, 1, ((modelica_integer) 1));
+^
+DrumBoilerModel_me_FMU_12jac.c:227:94: error: use of undeclared identifier '_omcQ_24TMP_5F424'
+jacobian->resultVars[1] /* der(fmi_x.$pDERA.dummyVarA[2]) JACOBIAN_VAR */ = real_array_get(_omcQ_24TMP_5F424, 1, ((modelica_integer) 2));
+^
+DrumBoilerModel_me_FMU_12jac.c:242:94: error: use of undeclared identifier '_omcQ_24TMP_5F424'
+jacobian->resultVars[2] /* der(fmi_x.$pDERA.dummyVarA[3]) JACOBIAN_VAR */ = real_array_get(_omcQ_24TMP_5F424, 1, ((modelica_integer) 3));
+^
+4 errors generated.
+make: *** [<builtin>: DrumBoilerModel_me_FMU_12jac.o] Error 1
+"
+
+
+
+
+
+
+
+
Equation mismatch: omc-diff says:
----------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------Failed 'D' '"'
Line 2030: Text differs:
expected: resultFile = "DrumBoilerModel_me_FMU_res.mat",
got: resultFile = "",
== 1 out of 1 tests failed [openmodelica/cppruntime/fmu/modelExchange/2.0/testDrumBoiler.mos_temp5065, time: 52]