EBSILON®Professional Online Documentation
EbsScript / EbsScript Functions / Calculation Functions
In This Topic
    Calculation Functions
    In This Topic

    Calculation Functions

    These functions are used to perform EBSILON®Professional calculations.

    Name

    Purpose

    validatevalidateWitherror

    Arguments

    Return Value

    Example

    Comments

    binaryMixtureTable

    Access to the material tables for binary mixtures

    1: INTEGER: Function Id

    2: REAL: Arg1

    3: REAL: Arg2

    4: INTEGER: Medium

    5: REAL: xi

    REAL

    var

       rH,rP,rT,rXi:real;
       iMedium:integer;

    begin          

       rP:=1;
       rT:=300;
       iMedium:=1; // NH3/H2O
       rXi:=0.9;
    // H (P,T)
       rH:=binaryMixtureTable(1001, rP, rT,
              Medium, rXi);

       println ("H =", rH,"\n");
    end.

     

    calcNCV

    Calculation of the calorific value

    1: STRING: Name of the pipe or component 1/33

    2: REAL: calorific value (result)

    BOOLEAN: true: o.k.

                      false: error

     

    var

         r,erg: real;

         ok: boolean;

    begin

          ok :=calcNCV("Value_7", erg);

    end

     

    clearAllCalculationErros

    Clears all error messages

    none

    none

    clearAllCalculationErrors;

     

    clearCalculationCache

    Clears the calculation cache
    for the Refprop- and the trend- DLL

    none

    none

     

    clearCalculationCache

     

    clearCalculationErrors

    Deletes the error messages of a profile

    1: INTEGER: Profile-Id
        (optional, Default = -1)

    none

     

    clearCalculationErrors(5)

     

    EbsIdent

    Executing an identification calculation for off-line systems: a new data set is appended in the data collection (.bel file), in case sufficient data sets are already available, then a new adaptation calculation is done. All the identifications are always calculated, which are contained in the configuration.

    None

    INTEGER

    0: OK.
    1: Cell already completely filled
    2: Still too less data sets for identification
    3: Area limits exceeded
    4: Error in adaptation calculation (Matrix singular)
    5: Internal error in area indexing
    6: .bel file does not match the identification
    7: Error in reading the .ref file
    8: Error in writing the .bel file
    9: Error in writing the .ref file
    14: Error in determining a variable
    15: Error in determining a coefficient
    16: Error in determining a target value

    i:=ebsIdent;

    Special license necessary

     

    EposNeuro

    Executing an identification calculation for online systems, handling similar to ebsIdent

    None

    INTEGER

    As in case of ebsIdent

    i:=eposNeuro;

    Special license necessary

    exit

    End the execution of the script.

    1: INTEGER: return code of the EbsScripts

    2: STRING: Notification string

    None

    exit (0);

    -

    fluegasTable

    Access to the material tables for fluids with specification of a material composition (always the complete composition is to be specified in the corresponding fields)

    1: INTEGER: Function-ID (see below)

    2: REAL: 1. Argument

    3: REAL: 2. Argument

    4: array of string: field with the names of the substances contained

    5: array of real: field with the mass fractions of the substances contained (in the same sequence as the names)

    6: INTEGER: size of the fields (4 and 5)

    7: INTEGER: CpMode-ID (see below)

    8: array * of: CpUser

    real: Result
     

    var
    rH,rP,rT:real
    arstrMaterialNameArray:array[0..1] of string;
    arrFractionArray:array[0..1] of real;
    nArraySize, CpMode-ID:integer;

    begin            

       rP:=1;

       rT:=300;

       arstrMaterialNameArray[0]:="N2";

       arstrMaterialNameArray[1]:="O2";

       arrFractionArray[0]:=0.75;

       arrFractionArray[1]:=0.25;

       nArraySize:=2;

       CpMode-ID:=1;

    // H (P,T)

       rH:=fluegasTable(1001, rP, rT, arstrMaterialNameArray, arrFractionArray, nArraySize, CpMode-ID);

       print ("H =", rH,"\n");

    // Conversion of mass-% in Vol-%

       fluegasTable(1023, rP, rT, arstrMaterialNameArray, arrFractionArray, nArraySize, CpMode-ID);

       print ("Volume fractions:",arrFractionArray[0]," ",arrFractionArray[1]);

    end.

     

    fluegasTable3

    Like fluegasTable, but with three  Arguments (required for feature-Ids 1053 and 1095, see below)

     

    1: INTEGER: Functions-Id (see below)

    2: REAL: 1. Argument

    3: REAL: 2. Argument

    4: REAL: 3. Argument

    5: array of string: Field with the names of the substances contained

    6: array of real: Field with the mass fractions of the substances contained (in the same order as the names)

    7: INTEGER: Size of the arrays (5 and 6)

    8: INTEGER: CpMode-Id (see below)

    9: array * of: CpUser

    REAL: Result
     

    		                

     

     

    getContext

    Retrieving the current context (name space) of the EbsScript

    -

    string: Kontextname
    ("::" = global context,
    "::Macro1::" = context of Macro1)

    str:=getContext;

     

    getStart Parameters

     

    Retrieving the start parameters that were specified when starting the EbsScript (e.g., from a button)

    1: INTEGER: Integer start parameter

    2:string: string start parameter

    None

    getStartParameters (i, str);

     

    identificationGetNames

    Retrieving the names of existing EbsIdent identifications

    1: array of STRING: names

     

    INTEGER: 0

     

     

    identificationGetResults

    Retrieving the results of an EbsIdent identification

    1: STRING: Name of identification

    2: array of REAL: coefficients

    3: array of REAL: standard deviations

    INTEGER: EbsIdent status
                   (see ebsIdent)

     

     

    identificationIdentify

    Performs an EbsIdent identification

    none

     

    INTEGER: EbsIdent status
                   (see ebsIdent)

     

     

    identificationInitialize

    Initializes the EbsIdent identification

    none

     

    INTEGER: EbsIdent status
                   (see ebsIdent)

     

     

    optimizeEasy

    Starting the optimizer with the default parameters.

    -

    BOOLEAN: true: OK
       false: Error

    optimizeEasy;

     

    optimizeGA

    Start the optimizer with the genetic algorithm

    1: INTEGER: Id, Index of the data set to be optimized

    2: INTEGER: maxTimeInSeconds = 0, maximum time that can be used for optimization - if 0, then no time limit

    		  Real: Result                   

    optimizeGA( 1,300);
    //Optimizes the data set with index 1 with a time limit of 5 minutes or less

     

    optimizeND

    Start the optimizer with the

    non-linear descent method algorithm

    1: INTEGER: Id, Index of the data set to be optimized

    2: INTEGER: maxTimeInSeconds = 0, maximum time that can be used for optimization - if 0, then no time limit

    Real: Result

    optimizeND(1 );
    //Optimizes the data set with index 1 (there is no time limit)

     

    propertyCallId

    Serves to call material value functions in equations ,that are issued by a KernelScript.

    1: INTEGER: Runtime object- ID (determined with getObjectSessionId)

    2: INTEGER: Function-Id (see below)

    3: REAL: 1. Argument

    4: REAL: 2. Argument

    5: REAL: value returned on error  (Default = -999)

    REAL: result

    utd:=ksgetspec(1);

    iIndex:=iIndex+1;

    strEquation:=printToString( "propcall(",

         getObjectSessionId( ksgetcomp._5 ),",",

         FuncT_of_PH, ",P5,H5) = ",

        "propcall(", getObjectSessionId ( ksgetcomp._9 ),  ",",

         FuncT_of_PH, ",P9,H9) + ",utd,"

        + 0.15*( H9 - value_of(H9))"

         );

    bOk:=ksSetEquation (iIndex,strEquation);

    (see Kernel_Scripting_9 in Examples\Components\Component_93.ebs)

     

    propertyCallObject

    Calling a substance value function for a specific object

    1: ebsData: Object

    2: FuncEnum: Function-Id, (see Interface-Unit System)

    3: REAL: 1. Argument

    4: REAL: 2. Argument

    5: REAL: value delivered in case of error (optional, Default = -999)

    REAL: result

    		  

    erg := propertyCallObject (Water,  FuncH_OF_PT,
               1,20);

     

    qualityFactors

    Calculating the quality factors

    1: INTEGER: ID of the identification according to the list prepared in the EbsIdent configuration

    2: REAL: calculated quality factor

    INTEGER

    0: OK.
    5: Internal error in area indexing
    6: .bel file does not match the identification
    7: Error in reading the .ref file
    10: Cell not occupied, but all variables in the valid range
    11: Not all variables in the valid range
    12: Faulty cell occupation
    13: Division by 0 while calculating the quality factors
    14: Error in determining a variable
    15: Error in determining a coefficient
    16: Error in determining a target value

    i:=qualityFactors (1,r);

     

    Special license necessary

     

    resetContext

    		 Resets the context
    (namespace) of an EbsScript

     

     

     

    		 sets current context :: MyMacro
    setContext (":: MyMacro");
    reset context (); // sets the context back                   

     

     

    SaltWaterTable

    Access to the material tables for salt water

    1: INTEGER: Function-ID (see below)

    2: REAL: 1. Argument

    3: REAL: 2. Argument

    4:REAL: Salt content (mass fraction of salt in the total mass)

    REAL: Result

    rH:=saltWaterTable(1001, 1.0, 20.0, 0.05 );

     

    setAdaptionPolynomial

    Sets the adjustment polynomial in a component

    1: STRING: component name

    2: STRING: Adaptation polynomial           

     

    none

    setAdaptionPolynomial ("Turbine","1+0.0001*T1");

     

    setCalculationComment

    Generates a comment for a specific object

    1: ebsObject: Object for which the comment is to be output.

    2: STRING: comment  

    none

    setCalculationComment (Water, "Pressure to high");

    only useful in the macro-EbsScript

    setCalculationError

    Generates an error message for a specific object and aborts the calculation if necessary.

    1: ebsObject: Object for which the error message is to be output.

    2: STRING: error text

    3: BOOLEAN (optional) :
       true (Default): breaking off 
       of  calculation
       false: no break

    none

    setCalculationWarning (Water, "Pressure to high",
    false ;);

    only useful in the macro-EbsScript
    (Argument 3 only relevant for EbsScript before starting the calculation)

    setCalculationWarning

    Generates a warning for a specific object

    1: ebsObject: Object for which the warning is to be issued.

    2: STRING: Text of the warning

    none

    setCalculationWarning (Water, "Pressure to high",
    false ;);

    only useful in the macro-EbsScript

    SetContext

    Setting the current context (name space) to the name of the specified macro

    1: string: name of the requested context) (e.g.,. "::Makro1::" or "::") or Macros (z.B. "Makro1")

     

    setContext("GT_24B");

    setContext("::GT_24B::");

    setContext("::");

     

    SetGlobalContext

    Resetting the current context back to the global namespace

    -

     

    setGlobalContext;

     

    Simulate

    Executing a simulation calculation (error appearing here are displayed only by the return code, an access to the error analysis is not possible in this function)

    None

    calculationResultEnum:

    0: Calculation successful

    1: Calculation ended with comments

    2: Calculation ended with warnings

    3: Calculation ended with errors

    4: Calculation not possible

    5: Fatal problem

    6: Accuracy not reached after maximum number of iterations, otherwise successful

    7: Accuracy not reached after maximum number of iterations, otherwise only warnings

    i:=simulate;

    -

    SimulateWith ErrorAnalysis

    Executing a simulation calculation with the possibility of a detailed error analysis. After the calculation ends, the error messages are present in the fields, which are transferred upon a call.

    1: array of string:
    Field with the names of the respective component or pipe affected by the error

    2: array of integer:
    Field with the class of the error that appears (see below)

    3: array of integer:
    Field with the type of the error

    4: array of string: Field with the description of the error type

    5: array of real: Field with additional information for the respective error (relevant only for double names)

    6: integer: available field size (to be transferred upon a call)

    7: integer: Number of errors found

    var

      arstrName:array[1..50] of string;

      arstrClass:array[1..50] of integer;

      arstrType:array[1..50] of integer;

      arstrDescription:array[1..50] of string;

      arstrValue:array[1..50] of real;

      iArraySize,iErrorCount:integer;

      i,iErr:integer;

    begin

      iArraySize:=50;

      iErr:=simulateWithErrorAnalysis (  arstrName, arstrClass, arstrType, arstrDescription, arstrValue,                                                          iArraySize, iErrorCount );

       for i:=1 to 50 do

       begin

         if (i<=iErrorCount) then

         begin

             print (arstrName[i]," ",arstrClass[i]," ",arstrType[i],

           " ",arstrDescription[i]," ",arstrValue[i],"\n");

         end;

       end;

       print ("iErr=",iErr,"  iErrorCount=",iErrorCount,"\n");

    end;

     

    SimulateWith ErrorAnalysisNew

    like simulateWith ErrorAnalysis, but using dynamical arrays

     

    1: array of CALCULATIONERROR

    calculationResultEnum:

    0: Calculation successful

    1: Calculation ended with comments

    2: Calculation ended with warnings

    3: Calculation ended with errors

    4: Calculation not possible

    5: Fatal problem

    6: Accuracy not reached after maximum number of iterations, otherwise successful

    7: Accuracy not reached after maximum number of iterations, otherwise only warnings

    var 

    iError:integer;
    errors : array of CALCULATIONERROR;

    i:integer; 

    begin

    iError:=simulateWithErrorAnalysisNew(errors); 

    if (iError > 1) then 

    begin 

    for i:=0 to length(errors)-1 do 

    begin 

     if (errors[i].errorLevel>1) then 

     begin 

     println (i," ",errors[i].errorClass," ",errors[i].errorLevel," ",errors[i].description); 

    end; 

    end; 

    end; 

    end;

    end;

     
    simulate_trans

    Die Funktion ermöglicht es, eine transiente Simulation mit dem vorgegebenen Zeitschritt in Sekunden und (optional) mit dem vorgegebenen Anfangs-Zeitpunkt durchzuführen.

    1: real: Zeitschritt in Sekunden

    2: real: Startzeit (optional)

    calculationResultEnum

    (siehe oben)

    start := "04.05.2020 00:00";
    rstart := convertTime (start);
    @calcoptions.sim.transientmode := 1;
    crc := simulate_trans_init(rstart);
    tsCopyDependentValues;

    @calcoptions.sim.transientmode := 2;
    crc := simulate_trans(5.0); // 5 Seconds
    tsCopyDependentValues;

    crc := simulate_trans(5.0);
    tsCopyDependentValues;
     
    crc := simulate_trans(5.0);
    tsCopyDependentValues;
    simulate_trans_init

    Die Funktion ermöglicht eine Initialisierungs-Simulation (analog zum ersten Schritt in der Zeitreihe) mit dem (optional) vorgegebenen Anfangs-Zeitpunkt.

    		 1: real: Startzeit (optional)

    calculationResultEnum

    (siehe oben)

    		 siehe oben (simulate_trans)

    transferAllResults

    Applies all results (for pipelines and components) from the specified profile to the current profile

    1: INTEGER: ID of the source profile

                   

     

    BOOLEAN

    transferAllResults(4);

     

    transferValResults

    For all measured values (component 46), takes the RESULT values from the specified profile as MEASM into the current profile

    1: INTEGER: ID of the source- profile

                   

     

    BOOLEAN

    transferValResults(4);

     

    user2PhaseTable

    Access to the material tables for the user-defined two-phase fluids

    1: INTEGER: Functions-ID (see below)

    2: REAL: 1. Argument

    3: REAL: 2. Argument

    4: INTEGER: Material-ID
    > 0: ID of a DLL provided by the user

    <0: according to FMED for component 1 or 33

    -1: Ammonia (NH3)

    -2: Water

    -3: Carbon dioxide (CO2)

    REAL: Result

    rH:=user2PhaseTable( 1001, 1.0, 20.0, -1);

     

    user2PhaseTable3

    Access to the material tables for the user-defined two-phase fluids

    1: INTEGER: Functions-Id (see below)

    2: REAL: 1. Argument

    3: REAL: 2. Argument

    4: REAL: 3. Argument

    5: INTEGER: Material-ID
    > 0:  ID of a DLL provided by the user

    <0: according to FMED for component 1 or 33

    REAL: Result

    xh2o:=user2PhaseTable3( 1053, 1.0, 20.0, 0.6, 4711
    (only for self-programmed DLL relevant, all internal   functions of the user2Phase panel come with two arguments)

     

     

     

    validate

    Executing a validation calculation

    None

    see simulate

    i:=validate;

    Special license necessary

    validateWithErrorAnalysis

    Executing a validation calculation with a detailed error analysis

    see simulateWith ErrorAnalysis

    similar to simulateWith ErrorAnalysis

    similar to simulateWith ErrorAnalysis

    Special license necessary

    validateWithErrorAnalysisNew

    like validateWith ErrorAnalysis, but using dynamical arrays

    1: array of CALCULATIONERROR

    see simulate

     

     

    waterSteam Table

    Access to the material tables for water or steam

    1: INTEGER: Functions-ID (see below)

    2: REAL: 1. Argument

    3: REAL: 2. Argument

    REAL: Result

    rH:=waterSteamTable(1001, rP, rT);

     

     

     

    Functions-IDs for the functions waterSteamTable, fluegasTable, binaryMixtureTable, saltWaterTable.

    Note: The FuncEnums are defined in the  "Interface Unit System" and are therefore always available in EbsScript.

    The functions called "diagrams only" were needed for the background images of the diagrams and may be implemented only in certain areas or sub-branches.   
        

    Number

    Function

    		 FuncEnum         

    Description

    Remarks on usability

     

    1001

    H (P,T)

    		 FuncH_OF_PT

    Enthalpy depending on pressure and temperature

    always

    1002

    S (P,T)

    		 FuncS_OF_PT

    Entropy depending on pressure and temperature

    always

    1003

    T (P,H)

    		 FuncT_OF_PH

    Temperature depending on pressure and enthalpy

    always

    1004

    T (P,S)

    		 FuncT_OF_PS

    Temperature depending on pressure and entropy

    always

    1005

    T' (P)

    		 FuncTBOIL_OF_P

    Temperature of the boiling liquid as a function of pressure (second argument is ignored)

    Not in the case of fluegasTable

    1006

    P' (T)

    		 FuncPBOIL_OF_T

    Pressure of the boiling liquid as a function of the temperature (second argument is ignored)

    Not in the case of fluegasTable

    1007

    H (P,S)

    		 FuncH_OF_PS

    Enthalpy depending on pressure and entropy

    always

    1008

    S (P,H)

    		 FuncS_OF_PH

    Entropy depending on pressure and enthalpy

    always

    1009

    X (P,H)

    		 FuncX_OF_PH

    Phase fraction as a function of pressure and enthalpy: 0 <= X <= 1: fraction of the gaseous phase in the two-phase region liquid / gaseous (X = 0: completely liquid, X = 1 completely gaseous) 10 <= X <= 11: increased by 10 Proportion of the liquid phase in the two-phase region solid / liquid (X = 10: completely solid, X = 11 completely liquid) 100 <= X <= 101: by 100 increased fraction of the gaseous phase in the two-phase region solid / gaseous (X = 100: completely solid , X = 101 completely gaseous)

    Not in the case of fluegasTable

    1010

     H' (P)

    		 FuncHBOIL_OF_P

    Enthalpy of the boiling liquid depending on the pressure

    Not in the case of fluegasTable

    1011

     H'' (P)

    		 FuncHDew_OF_P

    Enthalpy of the saturated gas depending on the pressure

    Not in the case of fluegasTable

    1012

    CP (P,H)

    		 FuncCP_OF_PH

    Isobaric specific heat depending on pressure and enthalpy

    always

    1013

    V (P,T)

    		 FuncV_OF_PT

    Specific volume depending on pressure and temperature

    always

    1014

    V (P,H)

    		 FuncV_OF_PH

    Specific volume depending on pressure and enthalpy

    always

    1015

    P (H')

    		 FuncPBOIL_OF_H

    Pressure as a function of the enthalpy of the boiling liquid (H ', X = 0)

    In the case of waterSteamTable;
    2-Phase liquid / gaseous Table
    and saltWaterTable

    1016

    P (S'')

    		 FuncPDew_OF_S

    Pressure as a function of the entropy of the saturated gas (S ", X = 1)

    In the case of waterSteamTable,
    2-Phase liquid / gaseous Table
    and saltWaterTable

    1017

    CP (P,T)

    		 FuncCP_OF_PT

    Isobaric specific heat depending on pressure and temperature

    always

    1018

    X (P,T)

    		 FuncX_OF_PT

    Mass fraction of the gaseous phase as a function of pressure and temperature

    always

    1019

    XH2Og_max (P,T)

    		 FuncXG_OF_PT

    Saturation limit: maximum possible proportion of gaseous water in a gaseous stream as a function of pressure and temperature

    Only in the case of fluegasTable

    1020

    MMOL_no_elem

    		 FuncMOLM_OF_MRAT

    Molecular weight (excluding the substances given as elementary analysis)

    always

    1021

    NCV

    		 FuncNCV_OF_MRAT

    Net calorific value

    always

    1022

    MOL_to_MASS

    		 FuncVRAT_TO_MRAT

    Conversion of mol fractions in mass fractions

    Only in the case of fluegasTable

    1023

    MASS_to_MOL_elem

    		 FuncMRAT_TO_VRAT

    Conversion of mass fractions into molar fractions (taking into account the substances given as elemental analysis)

    Only in the case of fluegasTable

    1024

    H (X,S) <deprecated>

    		 FuncH_OF_XS

    (Enthalpy as a function of vapour content and entropy

    (deprecated)

    was previously needed for creating charts, recursive calculation, only available in certain areas for waterSteamTable and binaryMixtureTable (only for NH3 / H2O)

    1025

    H (T,S) <deprecated>

    		 FuncH_OF_TS

    Enthalpy depending on temperature and entropy
    (deprecated)

    for watersteamtable, flue gastable and binarymixturetable (NH3 / H2O only)

    1026

    X (P,S)

    		 FuncX_OF_PS

    Steam content depending on pressure and entropy

    Not in the case of fluegasTable
                   

    1027

    P (X,S) <deprecated>

    		 FuncP_OF_XS

    Pressure depending on steam content and entropy
    (deprecated)

    only at waterSteamTable,  was created earlier
    needed from diagrams

    1028

    P (T,S) <deprecated>

    		 FuncP_OF_TS

    Pressure depending on temperature and entropy
    (deprecated)

    Only in the case of waterSteamTable
    and fluegasTable

    1029

    ETA (P,H)

    		 FuncETA_OF_PH

    Dynamic viscosity as a function of pressure and enthalpy

    always

    1030

    LAMBDA (P,H)

    		 FuncLAMBDA_OF_PH

    Thermal conductivity as a function of pressure and enthalpy

    always

    1031

    H (P,X)

    		 FuncH_OF_PX

    Enthalpy as a function of pressure and steam content

    waterSteamTable and                 user2PhaseTable

    1032

    MMOL_elem
    (all components)

    		 FuncMOLM1

    Molecular weight including all substances  (for internal conversions)

    always

    1033

    MMOL_elem
    (omitted)

    		 Funcdeprecated MII

    is eliminated

     

    1034

    equil 

    		 FuncPHASEEQ_PT

    (only for internal usage for updating the phase equilibrium)

    Only in the case of fluegasTable

    1035

    T (H,S)

    		 FuncT_OF_HS

    Temperature as a function of enthalpy and entropy

    for waterSteamTable and fluegasTable, user2PhaseTable and binaryMixureTable (NH3 / H2O only)

    1036

    T (X,S) <deprecated>

    		 FuncT_OF_XS

    Temperature as a function of steam mass fraction and entropy
    (deprecated)

    Only in the case of waterSteamTable,
                   

    1037

    P (S,H)

    		 FuncP_OF_SH

    Pressure as a function of entropy and enthalpy

    for waterSteamTable and fluegasTable, user2PhaseTable and binaryMixureTable (NH3 / H2O only)

    1038

    P (T,H) <not implemented>

    		 FuncP_OF_TH

    Pressure as a function of temperature and enthalpy 

     not usable

    1039

    P (X,H) <not implemented>

    		 FuncP_OF_XH

    Pressure as a function of steam content and enthalpy 

     not usable

    1040

    S (T,H)

    		 FuncP_FOF_TH

    Entropy as a function of temperature and enthalpy (function available in wet steam region only)

    only at waterSteamTable, user2PhaseTable in the two-phase region

    1041

    S (T,X)

    		 FuncS_OF_TX

    Entropy as a function of temperature and steam content

    only at waterSteamTable, user2PhaseTable in the two-phase region

    1042

    MASS_to_MOL_no_elem

    		 FuncMRAT_TO_VRAT1

    Conversion of mass fractions into parts by moles (without consideration of the substances given as elemental analysis

    Only in the case of fluegasTable

    1043

    XI' (P,T)

    		 FuncXI1_OF_PT

    Mass fraction of the refrigerant in the boiling liquid as a function of pressure and temperature

    only with binaryMixtureTable with NH3 / H2O and H2O / LiBr

    1044

    XI'' (P,T)

    		 FuncXI2_OF_PT

    Mass fraction of the refrigerant in the saturated vapour as a function of pressure and temperature

    only with binaryMixtureTable with NH3 / H2O and H2O / LiBr

    1045

    XI' (P,XI'')

    		 FuncXI1_OF_PXI2

    Mass fraction of the refrigerant in the boiling liquid as a function of pressure and mass fraction of the refrigerant in the saturated steam

    only with binaryMixtureTable with NH3 / H2O and H2O / LiBr

    1046

    XI'' (P,XI')

    		 FuncXI2_OF_PX1

    Mass fraction of the refrigerant in the saturated vapour as a function of pressure and mass fraction of the refrigerant in the boiling liquid

    only with binaryMixtureTable with NH3 / H2O and H2O / LiBr

    1047

    XI' (T,XI'')

    		 FuncXI1_OF_TXI2

    Mass fraction of the refrigerant in the boiling liquid as a function of temperature and mass fraction of the refrigerant in the saturated vapour

    only with binaryMixtureTable with NH3 / H2O and H2O / LiBr

    1048

    XI'' (T,XI')

    		 FuncXI2_OF_TXI1

    Mass fraction of the refrigerant in the saturated vapour as a function of temperature and mass fraction of the refrigerant in the boiling liquid

    only with binaryMixtureTable with NH3 / H2O and H2O / LiBr

    1049

    H_aux (PDEW)

    		 FuncHAUX_OF_PFG

    Enthalpy on the auxiliary line in the h-xi diagram, depending on the pressure

    only with binaryMixtureTable with NH3 / H2O and H2O / LiBr

    1050

    PH2O (P,T)

    		 FunPD_OF_PT

    Partial pressure of gaseous water present in the gaseous portion of the total flow as a function of pressure and temperature

    Only in the case of fluegasTable

    1051

    PH2O_max (P,T)

    		 FuncPDS_OF_PT

    Saturated steam pressure (= partial pressure at maximum possible proportion of gaseous water) of the water in the gaseous portion of the total flow as a function of pressure and temperature

    Only in the case of fluegasTable

    1052

    PHI (P,T)

    		 FuncPHI_OF_PT

    Relative humidity (to the water mass fraction XH2O given in the composition) as a function of pressure and temperature

    Only in the case of fluegasTable

    1053

    XH2O (P,T,PHI)

    		 FuncXIW_OF_PTPhi

    Water mass fraction XH2O as a function of pressure, temperature and relative humidity

    only at fluegasTable,
    needs three arguments
    (for reasons of compatibility also with two arguments and specification of the relative humidity as XH2O in the composition)

    1054

    Twb (P,T)

    		 FuncTWB_OF_PT

    Wet bulb temperature as a function of pressure and temperature

    Only in the case of fluegasTable

    1055

    T'' (P)

    		 FuncTDEW_OF_P

    Dew point temperature (condensation point of the saturated gas)
    or saturated steam temperature as a function of the pressure

    always

    1056

    H'(T)

    		 FuncHBOIL_OF_T

    Enthalpy of the boiling liquid (H ') as a function of the temperature

    not at fluegasTable

    1057

    H'' (T)

    		 FuncHDEW_OF_T

    Enthalpy of the saturated gas (H'') as a function of the temperature

    not at fluegasTable

    1058

    CV (P,T)

    		 FuncCV_OF_PT

    Specific isochoric heat capacity as a function of pressure and temperature

     

    always

    1059

    CV (P,H)

    		 FuncCV_OF_PH

    Specific iso chore specific heat capacity as a function of pressure and enthalpy

    always

    1060

    RHO (P,T)

    		 FuncRHO_OF_PT

    Density as a function of pressure and temperature

     

    always

    1061

    RHO (P,H)

    		 FuncRHO_OF_PH

    Density as a function of pressure and enthalpy

    always

    1062

    W (P,T)

    		 FuncW_OF_PT

    Isentropic sound velocity as a function of pressure and temperature

     

    always

    1063

    W (P,H)

    		 FuncW_OF_PH

    Isentropic sound velocity as a function of pressure and enthalpy

    always

    1064

    KAPPA (P,T)

    		 FuncKAPPA_OF_PT

    Adiabatic exponent as a function of pressure and temperature

    always

    1065

    KAPPA (P,H)

    		 FuncKAPPA_OF_PH

    Adiabatic exponent as a function of pressure and enthalpy

    always

    1066

    SIGMA (P')

    		 FuncSIGMA_OF_P

    Surface tension as a function of the boiling pressure

     

    only for waterSteamTable and only in the two-phase region

    1067

    SIGMA (T')

    		 FuncSIGMA_OF_T

    Surface tension as a function of the boiling temperature

    only for waterSteamTable and only in the two-phase region

    1068

    NUE (P,T)

    		 FuncNUE_OF_PT

    Kinematic viscosity as a function of pressure and temperature

    always

    1069

    NUE (P,H)

    		 FuncNUE_OF_PH

    Kinematic viscosity as a function of pressure and enthalpy

    always

    1070

    ETA (P,T)

    		 FuncETA_OF_PT

    Dynamic viscosity as a function of pressure and temperature

    always

    1071

    LAMDBA (P,T)

    		 FuncUNCH_OF_PT

    Thermal conductivity as a function of pressure and temperature

    always

    1072

    UNCH (P,T)  

    		 Funcdeprecated_UNCH_OF_PT

    Table uncertainty in enthalpy  (  is eliminated )

     

    1073

    Pcrit 

    		 FuncPCRIT_OF

    Critical pressure

    only for  waterSteamTable, user2PhaseTable and binaryMixtureTable

    1074

    Tcrit

    		 FuncTCRIT_OF

    Critical temperature

    only for  waterSteamTable, user2PhaseTable and binaryMixtureTable

    1075

    Tmin (const)

    		 FuncTMIN_OF_P

    Lower temperature limit

    Only in the case of waterSteamTable,  
    2-Phase liquid / gaseous Table,

    1076

    TMAX (const)

    		 FuncTMAX_OF_P

    Upper temperature limit

    always

    1077

    PMAX (const)

    		 FuncPMAX_OF_T

    Upper pressure limit

    always

    1078

    PHASE (P,H)

    		 FuncPHASE_OF_PH

    Phase from pressure and enthalpy

    2 for gaseous phase (in the one-phase region)

    4 for solid phase

    always

    1079

    P'' (H)

    		 FuncPDEW_OF_H

    Pressure, at which the gas at the saturation point (dew point) has the specified enthalpy

    only for user2PhaseTable with Refprop-
    Fluids

    1080

    P'' (T)

    		 FuncPDEW_OF_T

    Pressure, at which the gas at the saturation point (dew point) has the specified temperature

    always

    1081

    Pmelt (T)

    		 FuncPMEL_OF_T

    Melt pressure for ice as a function of temperature

    user2PhaseTable and saltWaterTable

    1082

    Tmelt (P)

    		 FuncTMEL_OF_P

    Melt pressure for ice as a function of pressure

    user2PhaseTable and saltWaterTable

    1083

    Psubl (T)

    		 FuncPSUB_OF_T

    Sublimation pressure as a function of the temperature for ice

    user2PhaseTable for H2O and CO2

    1084

    Tsubl (P)

    		 FuncTSUB_OF_P

    Sublimation temperature as a function of the pressure for ice

    user2PhaseTable for H2O and CO2

    1085

    Tfreeze (XI)

    		 FuncTFREEZE_OF_XI  Freezing temperature as a function of the mass fraction of the coolant

    Only in the case of binaryMixtureTable for
    FBIN<0 (LibSecRef)

    1086

    P (S')

    		 FuncTBOIL_OF_S

    Pressure as a function of the entropy of the boiling liquid

    only for user2PhaseTable with Refprop-
    Fluids

    1087

    T (H')

    		 FuncTBOIL_OF_H

    Temperature as a function of the enthalpy of the boiling liquid

    only for user2PhaseTable with Refprop-
    Fluids

    1088

    T (H'')

    		 FuncTDEW_OF_H

    Temperature as a function of the enthalpy of the saturated gas

    only for user2PhaseTable with Refprop-
    Fluids

    1089

    T (S')

    		 FuncTBOIL_OF_S

    Temperature as a function of the entropy of the boiling liquid

    only for user2PhaseTable with Refprop-
    Fluids

    1090

    T (S'')

    		 FuncTDEW_OF_S

    Temperature as a function of the entropy  of the saturated gas

    only for user2PhaseTable with Refprop-
    Fluids

    1091

    V (PX)

    		 FuncV_OF_PX

    Specific volume depending on pressure and vapour content

    only in the case of waterSteamTable  
                   

    1092

    V (TX)

    		 FuncV_OF_TX

    Specific volume as a function of temperature and vapour content

    only in the case of waterSteamTable  

    1093

    NCV (T)

    		 FuncNCV_OF_T

    Net calorific value depending on the reference temperature

    only in the case of flue gas Table

    1094

    PMIN (T)

    		 FuncPMIN_OF_T

    Lower pressure limit

    always

    1095

    XH2O (P,T,Tf)

    		 FuncXIW_OF_PTTf

    Water mass fraction as a function of pressure, temperature and wet bulb temperature

    at fluegasTable, requires 3 arguments

    1096

    XIMIN (P,H)

    		 FuncXMIN_OF_PH

    Minimum water content (crystallization limit LiBr) from pressure and enthalpy

    at user2PhaseTable with H2O / LiBr 

    1097

    XIMIN (T,H)

    		 FuncXMIN_OF_TH

    Minimum water content (crystallization limit LiBr) from temperature and enthalpy

    at user2PhaseTable with H2O / LiBr

    1098

    GCV (TREF)

    		 FuncGCV_OF_T

    Gross calorific value at given reference temperature

    flue gas Table

    1099

    NCV (GCV,TREF)

    		 FuncNCV_OF_T

    Net calorific value from gross calorific value at given reference temperature

    flue gas Table

    1100

    GCV (NCV,TREF)

    		 FuncGCV_OF_NCVT

    Gross calorific value from net calorific value at given reference temperature

    flue gas Table

    1101

    SATF (P,T)

    		 FuncSATF_OF_PT

    Saturation factor for the water mass fraction XH2O given in the composition as a function of pressure and temperature (for values <= 1 equal to the relative humidity, for values> 1 equal to the ratio of the actual water content to the maximum possible gaseous water content)
    (unlimited relative humidity)

    flue gas Table

    1102

    XCOMP (INDEX)

    		 FuncXCOMB_OF_IND

    Mass fraction for the substance designated by INDEX (INDEX = FSUBST according to component 45 or INDEX according to EbsScript -> Interface Unit System -> enumeration SubstanceEnum

    always

    1103

    PR (P,T)

    		 FuncPR_OF_PT

    Prandtl number depending on pressure and temperature

    always

    1104

    PR (P,H)

    		 FuncPR_OF_PH

    Prandtl number depending on pressure and enthalpy

    always

    1105

    HCRYST 

    		 FuncHCRYST_OF

    Crystallization Enthalpy

    at user2PhaseTable with H2O / LiBr

    1106

    PCRYST (T)

    		 FuncPCRYST_OF_T

    Crystallization Pressure depending on temperature

    at user2PhaseTable with H2O / LiBr

    1107

    TCRYST (P)

    		 FuncTCRYST_OF_P

    Crystallization Temperature depending on pressure

    at user2PhaseTable with H2O / LiBr

    1108

    XICRYST (P)

    		 FuncXICRYST_OF_P

    Cooling medium fraction at the crystallization limit as a function of the pressure

    at user2PhaseTable with H2O / LiBr

    1109

    XICRYST (T)

    		 FuncXICRYST_OF_T

    Cooling medium fraction at the crystallization limit as a function of the temperature

    at user2PhaseTable with H2O / LiBr

    1110

    H' (P,XI')

    		 FuncHBOIL_OF_PXIL

    Enthalpy of the boiling liquid (H ') at the saturation line as a function of the pressure and coolant content in the liquid phase (coolant is NH3 for NH3 / H2O, H2O for H2O / LiBr)

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1111

    H'' (P,XI')

    		 FuncHDEW_OF_PXIL Enthalpy of the saturated gas as a function of pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1112

    H' (T,XI')

    		 FuncHBOIL_OF_TXIL

    Enthalpy of the boiling liquid (H ') at the saturation line as a function of the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1113

    H'' (T,XI')

    		 FuncHDEW_OF_TXIL Enthalpy of the saturated gas as a function of temperature and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1114

    H' (P,XI'')

    		 FuncHBOIL_OF_PXIV

    Enthalpy of the boiling liquid as a function of the pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1115

    H'' (P,XI'')

    		 FuncHDEW_OF_PXIV Enthalpy of the saturated  gas as a function of the pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1116

    H' (T,XI'')

    		 FuncHBOIL_OF_TXIV

    Enthalpy of the boiling liquid (H ') as a function of the temperature and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1117

    H'' (T,XI'')

    		 FuncHDEW_OF_TXIV

    Enthalpy of the saturated gas as a function of the temperature and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1118

    H' (P,T)

    		 FuncHBOIL_OF_PT

    Enthalpy of the boiling liquid as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1119

    H'' (P.T)

    		 FuncHDEW_OF_PT

    Enthalpy of the saturated  gas as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1120

    S'  (P,XI')

    		 FuncSBOIL_OF_PXIL

    Entropy of the boiling liquid (S ') as a function of pressure and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1121

    S'' (P,XI')

    		 FuncSDEW_OF_PXIL

    Entropy of the saturated gas as a function of pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1122

    S' (T,XI')

    		 FuncSBOIL_OF_TXIL

    Entropy of the boiling liquid (S') as a function of temperature  and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1123

    S'' (T,XI')

    		 FuncSDEW_OF_TXIL

    Entropy of the saturated  gas (S'') as a function of temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr
    1124 S' (P,XI'') FuncSBOIL_OF_PXIV Entropy of the boiling liquid (S') as a function of pressure and coolant content in the gas phase at user2PhaseTable with NH3/H2O and H2O/LiBr

    1125

    S'' (P,XI'')

    		 FuncSDEW_OF_PXIV

    Entropy of the saturated  gas (S'') as a function of pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1126

    S' (T,XI'')

    		 FuncSBOIL_OF_TXIV

    Entropy of the boiling liquid (S') as a function of temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1127

    S'' (T,XI'')

    		 FuncSDEW_OF_TXIV

    Entropy of the saturated  gas (S'') as a function of temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1128

    S' (P,T)

    		 FuncSBOIL_OF_PT

    Entropy of the boiling liquid (S') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1129

    S'' (P,T)

    		 FuncSDEW_OF_PT

    Entropy of the saturated  gas (S'') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1130

    V' (P,XI')

    		 FuncVBOIL_OF_PXIL

    Specific volume of the boiling liquid (V ') as a function of the pressure and coolant proportion in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1131

    V'' (P,XI')

    		 FuncVDEW_OF_PXIL

    Specific volume of the saturated  gas (V'') as a function of the pressure and coolant proportion in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1132

    V' (T,XI')

    		 FuncVBOIL_OF_TXIL

    Specific volume of the boiling liquid (V ') as a function of the temperature and coolant proportion in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1133

    V'' (T,XI')

    		 FuncVDEW_OF_TXIL

    Specific volume of the saturated  gas (V'') as a function of the temperature and coolant proportion in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1134

    V' (P,XI'')

    		 FuncVBOIL_OF_PXIV

    Specific volume of the boiling liquid (V ') as a function of the pressure and coolant proportion in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1135

    V'' (P,XI'')

    		 FuncVDEW_OF_PXIV

    Specific volume of the saturated  gas (V'') as a function of the pressure and coolant proportion in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1136

    V' (T,XI'')

    		 FuncVBOIL_OF_TXIV

    Specific volume of the boiling liquid (V ') as a function of the temperature and coolant proportion in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1137

    V'' (T,XI'')

    		 FuncVDEW_OF_TXIV

    Specific volume of the saturated  gas (V'') as a function of the temperature and coolant proportion in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1138

    V' (P,T)

    		 FuncVBOIL_OF_PT

    Volume of the boiling liquid (V ') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1139

    V'' (P,T)

    		 FuncVDEW_OF_PT

    Volume of the saturated  gas (V'') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1140

    PR' (P,XI')

    		 FuncPRBOIL_OF_PXIL

    Prandtl number of boiling liquid (Pr ') as a function of the pressure and coolant fraction in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1141

    PR'' (P,XI')

    		 FuncPRDEW_OF_PXIL

    Prandtl number of saturated  gas (Pr'') as a function of the pressure and coolant fraction in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1142

    PR' (T,XI')

    		 FuncPRBOIL_OF_TXIL

    Prandtl number of boiling liquid (Pr ') as a function of the temperature and coolant fraction in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1143

    PR'' (T,XI')

    		 FuncPRDEW_OF_TXIL

    Prandtl number of saturated  gas (Pr'') as a function of the temperature and coolant fraction in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1144

    PR' (P,XI'')

    		 FuncPRBOIL_OF_PXIV

    Prandtl number of boiling liquid (Pr ') as a function of the pressure and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1145

    PR'' (P,XI'')

    		 FuncPRDEW_OF_PXIV

    Prandtl number of saturated  gas (Pr'') as a function of the pressure and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1146

    PR' (T,XI'')

    		 FuncPRBOIL_OF_TXIV

    Prandtl number of boiling liquid (Pr ') as a function of the temperature and coolant fraction in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1147

    PR'' (T,XI'')

    		 FuncPRDEW_OF_TXIV

    Prandtl number of saturated  gas (Pr'') as a function of the temperature and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1148

    PR' (P,T)

    		 FuncPRBOIL_OF_PT

    Prandtl number of the boiling liquid (Pr ') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1149

    PR'' (P,T)

    		 FuncPRDEW_OF_PT

    Prandtl number of the gaseous phase (Pr'') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1150

    CP' (P,XI')

    		 FuncCPBOIL_OF_PXIL

    Isobaric specific heat capacity of the boiling liquid (cp ') as a function of the pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1151

    CP'' (P,XI')

    		 FuncCPDEW_OF_PXIL

    Isobaric specific heat capacity of the saturated  gas  (cp'') as a function of the pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1152

    CP' (T,XI')

    		 FuncCPBOIL_OF_TXIL

    Isobaric specific heat capacity of the boiling liquid (cp ') as a function of the temperature and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1153

    CP'' (T,XI')

    		 FuncCPDEW_OF_TXIL

    Isobaric specific heat capacity of the saturated  gas  (cp'') as a function of the temperature and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1154

    CP' (P,XI'')

    		 FuncCPBOIL_OF_PXIV

    Isobaric specific heat capacity of the boiling liquid (cp') depending on the pressure and of the cooling agent fraction (gaseous)

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1155

    CP'' (P,XI'')

    		 FuncCPDEW_OF_PXIV

    Isobaric specific heat capacity of the saturated  gas  (cp'') as a function of the pressure and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1156

    CP' (T,XI'')

    		 FuncCPBOIL_OF_TXIV

    Isobaric specific heat capacity of the boiling liquid (cp')  depending on the temperature and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1157

    CP'' (T,XI'')

    		 FuncCPDEW_OF_TXIV

    Isobaric specific heat capacity of the saturated  gas  (cp'') as a function of the temperature and coolant fraction in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1158

    CP' (P,T)

    		 FuncCPBOIL_OF_PT

    Isobaric specific heat capacity of the boiling liquid (cp') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1159

    CP'' (P,T)

    		 FuncCPDEW_OF_PT

    Isobaric specific heat capacity of the gaseous phase  (cp'') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1160

    ETA' (P,XI')

    		 FuncETABOIL_OF_PXIL

    Dynamic viscosity of the boiling liquid (eta') depending on the pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1161

    ETA'' (P,XI')

    		 FuncETADEW_OF_PXIL

    Dynamic viscosity of the gaseous phase  (eta'')  depending on the pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1162

    ETA' (T,XI')

    		 FuncETABOIL_OF_TXIL

    Dynamic viscosity of the boiling liquid (eta')  depending on the temperature and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1163

    ETA'' (T,XI')

    		 FuncETADEW_OF_TXIL

    Dynamic viscosity of the gaseous phase  (eta'')  depending on the temperature and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1164

    ETA' (P,XI'')

    		 FuncETABOIL_OF_PXIV

    Dynamic viscosity of the boiling liquid (eta') depending on the pressure and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1165

    ETA'' (P,XI'')

    		 FuncETADEW_OF_PXIV

    Dynamic viscosity of the gaseous phase  (eta'')  depending on the pressure and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1166

    ETA' (T,XI'')

    		 FuncETABOIL_OF_TXIV

    Dynamic viscosity of the boiling liquid (eta') depending on the temperature and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1167

    ETA'' (T,XI'')

    		 FuncETADEW_OF_TXIV

    Dynamic viscosity of the gaseous phase  (eta'')  depending on the temperature and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1168

    ETA' (P,T)

    		 FuncETABOIL_OF_PT

    Dynamic viscosity of the boiling liquid (eta') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1169

    ETA'' (P,T)

    		 FuncETADEW_OF_PT

    Dynamic viscosity  of the gaseous phase  (eta'')  depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1170

    LAMDBA' (P,XI')

    		 FuncLAMBDABOIL_OF_PXIL

    Thermal conductivity of the boiling liquid (lambda') depending on the pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1171

    LAMDBA'' (P,XI')

    		 FuncLAMBDADEW_OF_PXIL

    Thermal conductivity of the gaseous phase  (lambda'')  depending on the pressure and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1172

    LAMDBA' (T,XI')

    		 FuncLAMBDABOIL_OF_TXIL

    Thermal conductivity of the boiling liquid (lambda') depending on the temperature and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1173

    LAMDBA'' (T,XI')

    		 FuncLAMBDADEW_OF_TXIL

    Thermal conductivity of the gaseous phase  (lambda'')  depending on the temperature and the proportion of coolant in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1174

    LAMDBA' (P,XI'')

    		 FuncLAMBDABOIL_OF_PXIV

    Thermal conductivity of the boiling liquid (lambda') depending on the pressure and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1175

    LAMDBA'' (P,XI'')

    		 FuncLAMBDADEW_OF_PXIV

    Thermal conductivity of the gaseous phase  (lambda'')  depending on the pressure and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1176

    LAMDBA' (T,XI'')

    		 FuncLAMBDABOIL_OF_TXIV

    Thermal conductivity of the boiling liquid (lambda') depending on the temperature and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1177

    LAMDBA'' (T,XI'')

    		 FuncLAMBDADEW_OF_TXIV

    Thermal conductivity of the gaseous phase  (lambda'')  depending on the temperature and the proportion of coolant in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1178

    LAMDBA' (P,T)

    		 FuncLAMBDABOIL_OF_PT

    Thermal conductivity of the boiling liquid (lambda') depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1179

    LAMDBA'' (P,T)

    		 FuncLAMBDADEW_OF_PT

    Thermal conductivity  of the gaseous phase  (lambda'')  depending on the pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1180

    NUE' (P,XI')

    		 FuncNUEBOIL_OF_PXIL

    Kinematic viscosity of the boiling liquid (nue ') as a function of the pressure and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1181

    NUE'' (P,XI')

    		 FuncNUEDEW_OF_PXIL

    Kinematic viscosity of the gaseous phase (nue '') as a function of the pressure and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1182

    NUE' (T,XI')

    		 FuncNUEBOIL_OF_TXIL

    Kinematic viscosity of the boiling liquid (nue') at the saturation line depending on the temperature and of the cooling agent fraction (liquid)

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1183

    NUE'' (T,XI')

    		 FuncNUEDEW_OF_TXIL

    Kinematic viscosity of the saturated gas (nue '') as a function of the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1184

    NUE' (P,XI'')

    		 FuncNUEBOIL_OF_PXIV

    Kinematic viscosity of the boiling liquid (nue ') as a function of the pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1185

    NUE'' (P,XI'')

    		 FuncNUEDEW_OF_PXIV

    Kinematic viscosity of the saturated gas (nue '') as a function of the pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1186

    NUE' (T,XI'')

    		 FuncNUEBOIL_OF_TXIV

    Kinematic viscosity of the boiling liquid (nue')  depending on the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1187

    NUE'' (T,XI'')

    		 FuncNUEDEW_OF_TXIV

    Kinematic viscosity of the saturated gas (nue '') as a function of the temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1188

    NUE' (P,T)

    		 FuncNUEBOIL_OF_PT

    Kinematic viscosity of the boiling liquid (nue ') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr,

    1189

    NUE'' (P,T)

    		 FuncNUEDEW_OF_PT

    Kinematic viscosity of the saturated gas (nue '') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1190

    CV' (P,XI')

    		 FuncCVBOIL_OF_PXIL

    Isochors specific heat capacity of the boiling liquid (cv ') as a function of pressure and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1191

    CV'' (P,XI')

    		 FuncCVDEW_OF_PXIL

    Isochors specific heat capacity of the gaseous phase  (cv'') 
    depending on the pressure and of the cooling agent fraction (liquid)

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1192

    CV' (T,XI')

    		 FuncCVBOIL_OF_TXIL

    Specific isochoric heat capacity of the boiling liquid (cv')  depending on the temperature and of the cooling agent fraction (liquid)

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1193

    CV'' (T.XI')

    		 FuncCVDEW_OF_TXIL

    Isochors specific heat capacity of the saturated gas (cv '') as a function of the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1194

    CV' (P,XI'')

    		 FuncCVBOIL_OF_PXIV

    Isochors specific heat capacity of the boiling liquid (cv ') as a function of pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1195

    CV'' (P,XI'')

    		 FuncCVDEW_OF_PXIV

    Isochors specific heat capacity of the saturated gas (cv '') as a function of pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1196

    CV' (T,XI'')

    		 FuncCVBOIL_OF_TXIV

    Specific isochoric heat capacity of the boiling liquid (cv')  as a function of the temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1197

    CV'' (T,XI'')

    		 FuncCVDEW_OF_TXIV

    Isochors specific heat capacity of the gaseous phase (cv '') as a function of the temperature and refrigerant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1198

    CV' (P,T)

    		 FuncCVBOIL_OF_PT

    Isochors specific heat capacity of the boiling liquid (cv ') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1199

    CV'' (P,T)

    		 FuncCVDEW_OF_PT

    Isochors specific heat capacity of the saturated gas (cv '') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1200

    W' (P,XI')

    		 FuncWBOIL_OF_PXIL

    Speed of sound of the boiling liquid (W ') as a function of pressure and refrigerant fraction in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1201

    W'' (P,XI')

    		 FuncWDEW_OF_PXIL

    Speed of sound of the saturated gas (w '') as a function of pressure and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1202

    W' (T,XI')

    		 FuncWBOIL_OF_TXIL

    Speed of sound of the boiling liquid (w ') as a function of the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1203

    W'' (T,XI')

    		 FuncWDEW_OF_TXIL

    Speed of sound of the saturated gas (w '') as a function of the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1204

    W' (P,XI'')

    		 FuncWBOIL_OF_PXIV

    Speed of sound of the boiling liquid (w ') as a function of pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1205

    W'' (P,XI'')

    		 FuncWDEW_OF_PXIV

    Speed of sound of the saturated gas (w '') as a function of pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1206

    W' (T,XI'')

    		 FuncWBOIL_OF_TXIV

    Speed of sound boiling liquid (w ') as a function of the temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1207

    W'' (T,XI'')

    		 FuncWDEW_OF_TXIV

    Speed of sound of the saturated gas (w '') as a function of the temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1208

    W' (P,T)

    		 FuncWBOIL_OF_PT

    Speed of sound of the boiling liquid (w ') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1209

    W'' (P,T)

    		 FuncWDEW_OF_PT

    Speed of sound of the saturated gas (w '') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1210

    KAPPA' (P,XI')

    		 FuncKAPPABOIL_OF_PXIL

    Adiabatic exponent of the boiling liquid (kappa') as a function of the pressure and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1211

    KAPPA'' (P,XI')

    		 FuncKAPPADEW_OF_PXIL

    Adiabatic exponent  of the gaseous phase  (kappa'') as a function of the pressure and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1212

    KAPPA' (T,XI')

    		 FuncKAPPABOIL_OF_TXIL

    Adiabatic exponent of the boiling liquid (kappa') depending on the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1213

    KAPPA'' (T,XI')

    		 FuncKAPPADEW_OF_TXIL

    Adiabatic exponent of the saturated gas (kappa '') as a function of the temperature and coolant content in the liquid phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1214

    KAPPA' (P,XI'')

    		 FuncKAPPABOIL_OF_PXIV

    Adiabatic exponent of the boiling liquid (kappa') as a function of the pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1215

    KAPPA'' (P,XI'')

    		 FuncKAPPADEW_OF_PXIV

    Adiabatic exponent  of the gaseous phase  (kappa'') as a function of the pressure and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1216

    KAPPA' (T,XI'')

    		 FuncKAPPABOIL_OF_TXIV

    Adiabatic exponent of the boiling liquid (kappa') as a function on the temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1217

    KAPPA'' (T,XI'')

    		 FuncKAPPADEW_OF_TXIV

    Adiabatic exponent  of sound of the gaseous phase  (kappa'') as a function on he temperature and coolant content in the gas phase

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1218

    KAPPA' (P,T)

    		 FuncKAPPABOIL_OF_PT

    Adiabatic exponent of the boiling liquid (kappa') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1219

    KAPPA'' (P,T)

    		 FuncKAPPADEW_OF_PT

    Adiabatic exponent  of saturated gas (kappa '') as a function of pressure and temperature

    at user2PhaseTable with NH3/H2O and H2O/LiBr

    1220

    T (P,PHI)

    		 FuncT_OF_PPHI

    Temperature, at which the current moisture content indicates the specified relative humidity

    (only with line type used "Humid air")

    1221

    Pdep (T)

    		 FuncPDEP_OF_T

    Deposition pressure (pressure above which the deposition of solid particles from the gas phase takes place) as a function of the temperature (for pure substances identical to sublimation temperature)

    at user2PhaseTable

    1222

    Tdep (P)

    		 FuncTDEP_OF_P

    Deposition temperature (temperature below which the deposition of solid particles from the gas phase takes place) as a function of the pressure (for pure substances identical to sublimation pressure)

    at user2PhaseTable

    In the physical properties libraries are available 107 functions from the 222 calculation functions which, although not yet used by Ebsilon, but are present in the substance value libraries.
    In particular, these are functions that calculate certain properties for given concentrations of the liquid and gaseous phase for mixtures. Of course, these functions can also be used with the corresponding EbsScript and EbsOpen calls.

     

    Ids (CpMode-Ids) for the function fluegasTable:

    The CpMode-ID defines which cp coefficients are to be used for the elemental analysis (C, H, O, N, S, Cl) content of the fluid:

    CpMode-Id

    Fluids

    1

    use flue gas coefficients

    2

    use gas coefficients

    3

    use coal coefficients due to type of coal FCOAL

    4

    use crude gas coefficients

    5

    use coefficients of oil (depending on ZFAC and RHOELEM)

    6

    Use user defined coefficients (Parameter array * of: cpUser)

    others

    Coefficients are set to 0

       

    Error classes for the functions simulateWithErrorAnalysis and ValidateWithErrorAnalysis:

    Class

    Meaning

    1

    Error in value specification (component 1 or 33)

    2

    Missing start value

    3

    Missing mass flow

    4

    Missing pressure

    5

    Missing enthalpy

    6

    Non-critical double naming in mass flow

    7

    Non-critical double-naming in pressure

    8

    Non-critical double-naming in enthalpy

    9

    (not used)

    10

    Negative mass flow

    11

    Negative pressure

    12

    Negative enthalpy

    13

    Component comments

    14

    Component warnings

    15

    Component errors

    16

    Relevant double naming in mass flow

    17

    Relevant double naming in pressure

    18

    Relevant double-naming in enthalpy

    19

    Low precision in mass flow

    20

    Low precision in pressure

    21

    Low precision in enthalpy

    22

    Expression could not be evaluated

    23

    No license for gas turbine macros

    24

    Error in validation of the mass flow

    25

    Error in validation of the pressure

    26

    Error in validation of the enthalpy

    27

    General pipe comment

    28

    General pipe warning

    29

    General pipe error

    30

    Missing net calorific value

    31

    Non-critical double-naming in net calorific value

    32

    Relevant double-naming in net calorific value

    33

    Error in validation of the net calorific value

    34

    Missing composition

    35

    Non-critical double-naming in the composition

    36

    Relevant double-naming in the composition

    37

    Error in validation of the composition

    38

    Maximal calculation time exceeded

    39

    Singular matrix in validation

    40

    Virtually singular matrix in validation

    41

    Cyclic logic line connection

    42

    Ambiguous logic line connection

    43

    Line that is set to "Do not calculate"

    44

    Uncritical double naming in frequency

    45

    Uncritical double naming in voltage

    46

    Uncritical double naming in the performance

    47

    Uncritical double naming in the phase

    48

    Relevant double naming in frequency

    49

    Relevant double naming in voltage

    50

    Relevant double naming in the performance

    51

    Relevant double naming in the phase 

    52

    Missing frequency

    53

    Missing voltage

    54

    Missing performance

    55

    Missing  phase 

     

     

     

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