SMath LLCSMath项目的作用域中创建。由smath发布。
这是一个开源项目。MIT许可证下共享的源代码SVN存储库

Features of WaterSteamPro

Functions (766 items):

  • wspCP1PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 1 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCP2PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 2 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCP3PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 3 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCP3RT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 3 [J/(kg·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspCP5PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 5 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCPEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific isobaric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspCPEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific isobaric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspCPHS("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspCPMSPT("1:argument", "2:argument") — Specific isobaric heat capacity of meta-stable supercooled steam [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCPPH("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspCPPS("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspCPPT("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCPPTX("1:argument", "2:argument", "3:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspCPSST("argument") — Specific isobaric heat capacity of steam at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCPSTX("1:argument", "2:argument") — Specific isobaric heat capacity in double-phase area [J/(kg·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspCPSWT("argument") — Specific isobaric heat capacity of water at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCV1PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 1 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCV2PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 2 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCV3PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 3 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCV3RT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 3 [J/(kg·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspCV5PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 5 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCVDPSST("argument") — Specific isochoric heat capacity of steam at saturation line from the double-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCVDPSWT("argument") — Specific isochoric heat capacity of water at saturation line from the double-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCVEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific isochoric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspCVEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific isochoric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspCVHS("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspCVMSPT("1:argument", "2:argument") — Specific isochoric heat capacity of meta-stable supercooled steam [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCVPH("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspCVPS("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspCVPT("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCVPTX("1:argument", "2:argument", "3:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspCVSST("argument") — Specific isochoric heat capacity of steam at saturation line from the one-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCVSTX("1:argument", "2:argument") — Specific isochoric heat capacity in double-phase area [J/(kg·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspCVSWT("argument") — Specific isochoric heat capacity of water at saturation line from the one-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspD1PT("1:argument", "2:argument") — Density in IF-97 region 1 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspD2PT("1:argument", "2:argument") — Density in IF-97 region 2 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspD3PT("1:argument", "2:argument") — Density in IF-97 region 3 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspD5PT("1:argument", "2:argument") — Density in IF-97 region 5 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDCPT("1:argument", "2:argument") — Static dielectric constant of ordinary water substance [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDCRT("1:argument", "2:argument") — Static dielectric constant of ordinary water substance [-] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspDDDHPPH("1:argument", "2:argument") — Derivate of density on enthalpy with constant pressure of water/steam [kg·sec2/m5] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspDDDHPPT("1:argument", "2:argument") — Derivate of density on enthalpy with constant pressure of water/steam [kg·sec2/m5] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDDDHPPTX("1:argument", "2:argument", "3:argument") — Derivate of density on enthalpy with constant pressure of water/steam [kg·sec2/m5] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDDDHPSST("argument") — Derivate of density on enthalpy with constant pressure of steam at saturation line [kg·sec2/m5] as function of temperature t "argument" [K].
  • wspDDDHPSWT("argument") — Derivate of density on enthalpy with constant pressure of water at saturation line [kg·sec2/m5] as function of temperature t "argument" [K].
  • wspDDDPHPH("1:argument", "2:argument") — Derivate of density on pressure with constant enthalpy of water/steam [sec2/m2] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspDDDPHPT("1:argument", "2:argument") — Derivate of density on pressure with constant enthalpy of water/steam [sec2/m2] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDDDPHPTX("1:argument", "2:argument", "3:argument") — Derivate of density on pressure with constant enthalpy of water/steam [sec2/m2] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDDDPHSST("argument") — Derivate of density on pressure with constant enthalpy of steam at saturation line [sec2/m2] as function of temperature t "argument" [K].
  • wspDDDPHSWT("argument") — Derivate of density on pressure with constant enthalpy of water at saturation line [sec2/m2] as function of temperature t "argument" [K].
  • wspDPDTST("argument") — Derivative of saturation pressure on saturation temperature [Pa/K] as function of temperature t "argument" [K].
  • wspDPT("1:argument", "2:argument") — Density [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDPTX("1:argument", "2:argument", "3:argument") — Density [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDSST("argument") — Density of steam at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspDSTX("1:argument", "2:argument") — Density in double-phase area [kg/m3] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspDSWT("argument") — Density of water at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspDYNVISEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Dynamic viscosity at the end of expansion/compression process [Pa·sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspDYNVISEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Dynamic viscosity at the end of expansion/compression process [Pa·sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspDYNVISHS("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspDYNVISMSPT("1:argument", "2:argument") — Dynamic viscosity of meta-stable supercooled steam [Pa·sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDYNVISPH("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspDYNVISPS("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspDYNVISPT("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDYNVISPTX("1:argument", "2:argument", "3:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDYNVISRT("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspDYNVISSST("argument") — Dynamic viscosity of steam at saturation line [Pa·sec] as function of temperature t "argument" [K].
  • wspDYNVISSTX("1:argument", "2:argument") — Dynamic viscosity in double-phase area [Pa·sec] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspDYNVISSWT("argument") — Dynamic viscosity of water at saturation line [Pa·sec] as function of temperature t "argument" [K].
  • wspgADDGASM("1:argument", "2:argument", "3:argument") — Addition of one gas to another as function of identificator of target gas [-], identificator of added gas "1:argument" [-], added gas mass "2:argument" [-].
  • wspgADDGASV("1:argument", "2:argument", "3:argument") — Addition of one gas to another as function of identificator of target gas [-], identificator of added gas "1:argument" [-], added gas volume "2:argument" [-].
  • wspgCPGST("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgCPIDT("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgCVGST("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgCVIDT("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgDELETEGASES("argument") — Deleting of all user-defined gases.
  • wspgDELETEGASID("argument") — Deleting of early created gas as function of gas identificator [-].
  • wspGETABSOLUTEGASCONSTANT("argument") — Absolute gas constant [J/(mole·K)].
  • wspGETCHECKRANGEMODE("argument") — Mode of checking the range of functions arguments.
  • wspGETDELTAPRESSURE("argument") — Maximum difference between pressure values at estimation of the area 3 parameters [Pa].
  • wspGETDELTATS("argument") — Maximum difference between saturation temperature and input temperature for function wspWATERSTATEAREA [K].
  • wspGETINITSTEAMDENSITY("argument") — Initial value for density of steam in IF-97 region 3 [kg/m3].
  • wspGETINITWATERDENSITY("argument") — Initial value for density of water in IF-97 region 3 [kg/m3].
  • wspGETLASTERROR("argument") — Last error code.
  • wspGETLASTERRORDESCRIPTION("argument") — Last error description.
  • wspGETLASTERRORDESCRIPTIONW("argument") — Last error description.
  • wspGETMAXITERATION("argument") — Maximum iterations count for Newton method.
  • wspGETTOLERANCE("argument") — Relative precision in the WaterSteamPro functions [-].
  • wspGETTOLERANCEMODE("argument") — Mode of management of make function results more precise.
  • wspGETWSPVERSION("argument") — Internal version of the WaterSteamPro.
  • wspgGASESCOUNT("argument") — Available gases count.
  • wspgGCGS("argument") — Specific gas constant [J/(kg·K)] as function of gas specification "argument" [-].
  • wspgGCID("argument") — Specific gas constant [J/(kg·K)] as function of gas identificator "argument" [-].
  • wspgGETCALCDISSMODE("argument") — Mode of calculating dissociation while calculate gases mixtures.
  • wspgHGST("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgHIDT("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgIDNAME("argument") — Gas identificator as function of existing gas name [-].
  • wspgMFGSGS("1:argument", "2:argument") — Mass fraction (MF) of gas as function of primary gas specification [-], gas specification looked for "1:argument" [-].
  • wspgMFIDID("1:argument", "2:argument") — Mass fraction (MF) of gas as function of primary gas identificator [-], gas identificator looked for "1:argument" [-].
  • wspgMMGS("argument") — Molar mass [kg/mole] as function of gas specification "argument" [-].
  • wspgMMID("argument") — Molar mass [kg/mole] as function of gas identificator "argument" [-].
  • wspgNEWID("argument") — New gas identificator.
  • wspgNEWIDGS("argument") — New gas identificator as function of gas specification [-].
  • wspgNEWIDNAME("argument") — Gas identificator as function of new gas name [-].
  • wspgPGSTS("1:argument", "2:argument", "3:argument") — Pressure [Pa] as function of gas specification "1:argument" [-], temperature t "2:argument" [K], specific entropy s "3:argument" [J/(kg·K)].
  • wspgPIDTS("1:argument", "2:argument", "3:argument") — Pressure [Pa] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K], specific entropy s "3:argument" [J/(kg·K)].
  • wspgSETCALCDISSMODE("argument") — Set and return a mode of calculating dissociation while calculate gases mixtures as function of mode [-].
  • wspgSGSPT("1:argument", "2:argument", "3:argument") — Specific entropy [J/(kg·K)] as function of gas specification "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgSGST("1:argument", "2:argument") — Specific entropy at pressure p0 = 100 kPa [J/(kg·K)] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgSIDPT("1:argument", "2:argument", "3:argument") — Specific entropy [J/(kg·K)] as function of gas identificator "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgSIDT("1:argument", "2:argument") — Specific entropy at pressure p0 = 100 kPa [J/(kg·K)] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgTGSH("1:argument", "2:argument") — Temperature [K] as function of gas specification "1:argument" [-], specific enthalpy h "2:argument" [J/kg].
  • wspgTGSPS("1:argument", "2:argument", "3:argument") — Temperature [K] as function of gas specification "1:argument" [-], pressure p "2:argument" [Pa], specific entropy s "3:argument" [J/(kg·K)].
  • wspgTGSS("1:argument", "2:argument") — Temperature at pressure p0 = 100 kPa [K] as function of gas specification "1:argument" [-], specific entropy s "2:argument" [J/(kg·K)].
  • wspgTIDH("1:argument", "2:argument") — Temperature [K] as function of gas identificator "1:argument" [-], specific enthalpy h "2:argument" [J/kg].
  • wspgTIDPS("1:argument", "2:argument", "3:argument") — Temperature [K] as function of gas identificator "1:argument" [-], pressure p "2:argument" [Pa], specific entropy s "3:argument" [J/(kg·K)].
  • wspgTIDS("1:argument", "2:argument") — Temperature at pressure p0 = 100 kPa [K] as function of gas identificator "1:argument" [-], specific entropy s "2:argument" [J/(kg·K)].
  • wspgUGST("1:argument", "2:argument") — Specific internal energy [J/kg] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgUIDT("1:argument", "2:argument") — Specific internal energy [J/kg] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgVFGSGS("1:argument", "2:argument") — Volume fraction (VF) of gas as function of primary gas specification [-], gas specification looked for "1:argument" [-].
  • wspgVFIDID("1:argument", "2:argument") — Volume fraction (VF) of gas as function of primary gas identificator [-], gas identificator looked for "1:argument" [-].
  • wspgVGSPT("1:argument", "2:argument", "3:argument") — Specific volume [m3/kg] as function of gas specification "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgVGST("1:argument", "2:argument") — Specific volume at pressure p0 = 100 kPa [m3/kg] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgVIDPT("1:argument", "2:argument", "3:argument") — Specific volume [m3/kg] as function of gas identificator "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgVIDT("1:argument", "2:argument") — Specific volume at pressure p0 = 100 kPa [m3/kg] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspH1PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 1 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspH2B2CP("argument") — Specific enthalpy at line between areas 2b and 2c [J/kg] as function of pressure p "argument" [Pa].
  • wspH2PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 2 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspH3PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 3 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspH3RT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 3 [J/kg] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspH5PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 5 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspHB13S("argument") — Specific enthalpy at boundary line between areas 1 and 3 [J/kg] as function of specific entropy s "argument" [J/(kg·K)].
  • wspHEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific enthalpy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspHEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific enthalpy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspHMSPT("1:argument", "2:argument") — Specific enthalpy of meta-stable supercooled steam [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspHPS("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspHPT("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspHPTX("1:argument", "2:argument", "3:argument") — Specific enthalpy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspHSST("argument") — Specific enthalpy of steam at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspHSTX("1:argument", "2:argument") — Specific enthalpy in double-phase area [J/kg] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspHSWT("argument") — Specific enthalpy of water at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspJOULETHOMPSON1PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 1 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSON2PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 2 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSON3PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 3 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSON3RT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 3 [K/Pa] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspJOULETHOMPSON5PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 5 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSONEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Joule-Thomson coefficient at the end of expansion/compression process [K/Pa] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspJOULETHOMPSONEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Joule-Thomson coefficient at the end of expansion/compression process [K/Pa] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspJOULETHOMPSONHS("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspJOULETHOMPSONMSPT("1:argument", "2:argument") — Joule-Thomson coefficient of meta-stable supercooled steam [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSONPH("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspJOULETHOMPSONPS("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspJOULETHOMPSONPT("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSONPTX("1:argument", "2:argument", "3:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspJOULETHOMPSONSST("argument") — Joule-Thomson coefficient of steam at saturation line [K/Pa] as function of temperature t "argument" [K].
  • wspJOULETHOMPSONSTX("1:argument", "2:argument") — Joule-Thomson coefficient in double-phase area [K/Pa] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspJOULETHOMPSONSWT("argument") — Joule-Thomson coefficient of water at saturation line [K/Pa] as function of temperature t "argument" [K].
  • wspKEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Isoentropic exponent at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspKEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Isoentropic exponent [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspKHS("1:argument", "2:argument") — Isoentropic exponent [-] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspKINVISEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Kinematic viscosity at the end of expansion/compression process [m2/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspKINVISEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Kinematic viscosity at the end of expansion/compression process [m2/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspKINVISHS("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspKINVISMSPT("1:argument", "2:argument") — Kinematic viscosity of meta-stable supercooled steam [m2/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKINVISPH("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspKINVISPS("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspKINVISPT("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKINVISPTX("1:argument", "2:argument", "3:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspKINVISSST("argument") — Kinematic viscosity of steam at saturation line [m2/sec] as function of temperature t "argument" [K].
  • wspKINVISSTX("1:argument", "2:argument") — Kinematic viscosity in double-phase area [m2/sec] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspKINVISSWT("argument") — Kinematic viscosity of water at saturation line [m2/sec] as function of temperature t "argument" [K].
  • wspKMSPT("1:argument", "2:argument") — Isoentropic exponent of meta-stable supercooled steam [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKPH("1:argument", "2:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspKPS("1:argument", "2:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspKPT("1:argument", "2:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKPTX("1:argument", "2:argument", "3:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspKSST("argument") — Isoentropic exponent of steam at saturation line [-] as function of temperature t "argument" [K].
  • wspKSTX("1:argument", "2:argument") — Isoentropic exponent in double-phase area [-] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspKSWT("argument") — Isoentropic exponent of water at saturation line [-] as function of temperature t "argument" [K].
  • wspLOCALREGISTRATIONEXA("1:argument", "2:argument") — Process registration of the WaterSteamPro as function of registration name [-], registration data "1:argument" [-].
  • wspLOCALREGISTRATIONEXW("1:argument", "2:argument") — Process registration of the WaterSteamPro as function of registration name [-], registration data "1:argument" [-].
  • wspP1HS("1:argument", "2:argument") — Pressure in IF-97 region 1 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspP23T("argument") — Pressure at line between areas 2 and 3 [Pa] as function of temperature t "argument" [K].
  • wspP2B2CH("argument") — Pressure at line between areas 2b and 2c [Pa] as function of specific enthalpy h "argument" [J/kg].
  • wspP2HS("1:argument", "2:argument") — Pressure in IF-97 region 2 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspP3HS("1:argument", "2:argument") — Pressure in IF-97 region 3 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspP3RT("1:argument", "2:argument") — Pressure in IF-97 region 3 [Pa] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspP5HS("1:argument", "2:argument") — Pressure in IF-97 region 5 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPB23HS("1:argument", "2:argument") — Pressure at boundary line between areas 2 and 3 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPHASESTATEPT("1:argument", "2:argument") — Area of phase state as function of pressure p [Pa], temperature t "1:argument" [K].
  • wspPHS("1:argument", "2:argument") — Pressure [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPKWPT("1:argument", "2:argument") — Negative logarithm (base 10) of the ionization constant of water [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspPKWRT("1:argument", "2:argument") — Negative logarithm (10 base) of the ionization constant of water [-] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspPMELTIT("argument") — Pressure at melting line of ice I [Pa] as function of temperature t "argument" [K].
  • wspPRANDTLEEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Prandtl number at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspPRANDTLEEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Prandtl number at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspPRANDTLEHS("1:argument", "2:argument") — Prandtl number [-] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPRANDTLEMSPT("1:argument", "2:argument") — Prandtl number of meta-stable supercooled steam [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspPRANDTLEPH("1:argument", "2:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspPRANDTLEPS("1:argument", "2:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspPRANDTLEPT("1:argument", "2:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspPRANDTLEPTX("1:argument", "2:argument", "3:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspPRANDTLESST("argument") — Prandtl number of steam at saturation line [-] as function of temperature t "argument" [K].
  • wspPRANDTLESTX("1:argument", "2:argument") — Prandtl number in double-phase area [-] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspPRANDTLESWT("argument") — Prandtl number of water at saturation line [-] as function of temperature t "argument" [K].
  • wspPST("argument") — Pressure at saturation line [Pa] as function of temperature t "argument" [K].
  • wspPSUBT("argument") — Pressure at sublimation line [Pa] as function of temperature t "argument" [K].
  • wspR3PT("1:argument", "2:argument") — Density in IF-97 region 3 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspR3PTR0("1:argument", "2:argument", "3:argument") — Density in IF-97 region 3 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], initial density r0 "3:argument" [kg/m3].
  • wspRIPTL("1:argument", "2:argument", "3:argument") — Refractive index [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], wave length wavelength "3:argument" [m].
  • wspRIRTL("1:argument", "2:argument", "3:argument") — Refractive index [-] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K], wave length wavelength "3:argument" [m].
  • wspROUGHHSSS("argument") — Specific enthalpy of steam at saturation line [J/kg] as function of specific entropy s "argument" [J/(kg·K)].
  • wspROUGHHSWS("argument") — Specific enthalpy of water at saturation line [J/kg] as function of specific entropy s "argument" [J/(kg·K)].
  • wspROUGHRSST("argument") — Rough value of density of steam at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspROUGHRSWT("argument") — Rough value of density of water at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspRST("argument") — Specific evaporation heat [J/kg] as function of temperature t "argument" [K].
  • wspS1PT("1:argument", "2:argument") — Specific entropy in IF-97 region 1 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspS2PT("1:argument", "2:argument") — Specific entropy in IF-97 region 2 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspS3PT("1:argument", "2:argument") — Specific entropy in IF-97 region 3 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspS3RT("1:argument", "2:argument") — Specific entropy in IF-97 region 3 [J/(kg·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspS5PT("1:argument", "2:argument") — Specific entropy in IF-97 region 5 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspSETCHECKRANGEMODE("argument") — Set and return a mode of checking the range of functions arguments as function of mode [-].
  • wspSETDELTAPRESSURE("argument") — Set and return maximum difference between pressure values at estimation of the area 3 parameters [Pa] as function of delta pressure delta "argument" [Pa].
  • wspSETDELTATS("argument") — Set and return maximum difference between saturation temperature and input temperature for function wspWATERSTATEAREA [K] as function of temperature delta "argument" [_K].
  • wspSETINITSTEAMDENSITY("argument") — Set and return the initial value for density of steam in IF-97 region 3 [kg/m3] as function of density r "argument" [kg/m3].
  • wspSETINITWATERDENSITY("argument") — Set and return initial value for density of water in IF-97 region 3 [kg/m3] as function of density r "argument" [kg/m3].
  • wspSETLASTERROR("argument") — Set and return a last error code as function of error code [-].
  • wspSETMAXITERATION("argument") — Set and return maximum iterations count for Newton method as function of maximum iteration [-].
  • wspSETTOLERANCE("argument") — Set and return relative precision in the WaterSteamPro functions [-] as function of tolerance "argument" [_-].
  • wspSETTOLERANCEMODE("argument") — Set and return a mode of management of make function results more precise as function of mode [-].
  • wspSEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific entropy at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspSEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific entropy at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspSMSPT("1:argument", "2:argument") — Specific entropy of meta-stable supercooled steam [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspSPH("1:argument", "2:argument") — Specific entropy [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspSPT("1:argument", "2:argument") — Specific entropy [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspSPTX("1:argument", "2:argument", "3:argument") — Specific entropy [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspSSST("argument") — Specific entropy of steam at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspSSTX("1:argument", "2:argument") — Specific entropy in double-phase area [J/(kg·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspSSWT("argument") — Specific entropy of water at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspSURFTENT("argument") — Surface tension [N/m] as function of temperature t "argument" [K].
  • wspT1HS("1:argument", "2:argument") — Temperature in IF-97 region 1 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT1PH("1:argument", "2:argument") — Temperature in IF-97 region 1 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT1PS("1:argument", "2:argument") — Temperature in IF-97 region 1 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT23P("argument") — Temperature at line between areas 2 and 3 [K] as function of pressure p "argument" [Pa].
  • wspT2APH("1:argument", "2:argument") — Temperature in IF-97 region 2a [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2APS("1:argument", "2:argument") — Temperature in IF-97 region 2a [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2BPH("1:argument", "2:argument") — Temperature in IF-97 region 2b [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2BPS("1:argument", "2:argument") — Temperature in IF-97 region 2b [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2CPH("1:argument", "2:argument") — Temperature in IF-97 region 2c [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2CPS("1:argument", "2:argument") — Temperature in IF-97 region 2c [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2HS("1:argument", "2:argument") — Temperature in IF-97 region 2 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2PH("1:argument", "2:argument") — Temperature in IF-97 region 2 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2PS("1:argument", "2:argument") — Temperature in IF-97 region 2 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT3HS("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT3PH("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT3PS("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT3RH("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of density r "1:argument" [kg/m3], specific enthalpy h "2:argument" [J/kg].
  • wspT5HS("1:argument", "2:argument") — Temperature in IF-97 region 5 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT5PH("1:argument", "2:argument") — Temperature in IF-97 region 5 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT5PS("1:argument", "2:argument") — Temperature in IF-97 region 5 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspTB23HS("1:argument", "2:argument") — Temperature at boundary line between areas 2 and 3 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Temperature at the end of expansion/compression process [K] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspTEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Temperature at the end of expansion/compression process [K] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspTHERMCONDEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Thermal conductivity coefficient at the end of expansion/compression process [W/(m·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspTHERMCONDEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Thermal conductivity coefficient at the end of expansion/compression process [W/(m·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspTHERMCONDHS("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTHERMCONDMSPT("1:argument", "2:argument") — Thermal conductivity coefficient of meta-stable supercooled steam [W/(m·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspTHERMCONDPH("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspTHERMCONDPS("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspTHERMCONDPT("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspTHERMCONDPTX("1:argument", "2:argument", "3:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspTHERMCONDRT("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspTHERMCONDSST("argument") — Thermal conductivity coefficient of steam at saturation line [W/(m·K)] as function of temperature t "argument" [K].
  • wspTHERMCONDSTX("1:argument", "2:argument") — Thermal conductivity coefficient in double-phase area [W/(m·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspTHERMCONDSWT("argument") — Thermal conductivity coefficient of water at saturation line [W/(m·K)] as function of temperature t "argument" [K].
  • wspTHS("1:argument", "2:argument") — Temperature [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTPH("1:argument", "2:argument") — Temperature [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspTPS("1:argument", "2:argument") — Temperature [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspTSHS("1:argument", "2:argument") — Temperature at saturation line [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTSP("argument") — Temperature at saturation line [K] as function of pressure p "argument" [Pa].
  • wspU1PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 1 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspU2PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 2 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspU3PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 3 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspU3RT("1:argument", "2:argument") — Specific internal energy in IF-97 region 3 [J/kg] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspU5PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 5 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspUEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific internal energy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspUEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific internal energy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspUHS("1:argument", "2:argument") — Specific internal energy [J/kg] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspUMSPT("1:argument", "2:argument") — Specific internal energy of meta-stable supercooled steam [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspUPH("1:argument", "2:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspUPS("1:argument", "2:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspUPT("1:argument", "2:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspUPTX("1:argument", "2:argument", "3:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspUSST("argument") — Specific internal energy of steam at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspUSTX("1:argument", "2:argument") — Specific internal energy in double-phase area [J/kg] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspUSWT("argument") — Specific internal energy of water at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspV1PT("1:argument", "2:argument") — Specific volume in IF-97 region 1 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspV2PT("1:argument", "2:argument") — Specific volume in IF-97 region 2 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspV3HS("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspV3PH("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspV3PS("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspV3PT("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspV5PT("1:argument", "2:argument") — Specific volume in IF-97 region 5 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspVEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific volume at the end of expansion/compression process [m3/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspVEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific volume at the end of expansion/compression process [m3/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspVHS("1:argument", "2:argument") — Specific volume [m3/kg] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspVMSPT("1:argument", "2:argument") — Specific volume of meta-stable supercooled steam [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspVPH("1:argument", "2:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspVPS("1:argument", "2:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspVPT("1:argument", "2:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspVPTX("1:argument", "2:argument", "3:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspVSST("argument") — Specific volume of steam at saturation line [m3/kg] as function of temperature t "argument" [K].
  • wspVSTX("1:argument", "2:argument") — Specific volume in double-phase area [m3/kg] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspVSWT("argument") — Specific volume of water at saturation line [m3/kg] as function of temperature t "argument" [K].
  • wspW1PT("1:argument", "2:argument") — Sound velocity in IF-97 region 1 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspW2PT("1:argument", "2:argument") — Sound velocity in IF-97 region 2 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspW3PT("1:argument", "2:argument") — Sound velocity in IF-97 region 3 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspW3RT("1:argument", "2:argument") — Sound velocity in IF-97 region 3 [m/sec] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspW5PT("1:argument", "2:argument") — Sound velocity in IF-97 region 5 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspWATERSTATEAREA("1:argument", "2:argument") — IF-97 region as function of pressure p [Pa], temperature t "1:argument" [K].
  • wspWATERSTATEAREA2("1:argument", "2:argument") — IF-97 region (version 2) as function of pressure p [Pa], temperature t "1:argument" [K].
  • wspWATERSTATEAREAHS("1:argument", "2:argument") — IF-97 region as function of specific enthalpy h [J/kg], specific entropy s "1:argument" [J/(kg·K)].
  • wspWATERSTATEAREAPH("1:argument", "2:argument") — IF-97 region as function of pressure p [Pa], specific enthalpy h "1:argument" [J/kg].
  • wspWATERSTATEAREAPS("1:argument", "2:argument") — IF-97 region as function of pressure p [Pa], specific entropy s "1:argument" [J/(kg·K)].
  • wspWEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Sound velocity at the end of expansion/compression process [m/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspWEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Sound velocity at the end of expansion/compression process [m/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspWHS("1:argument", "2:argument") — Speed of sound [m/sec] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspWMSPT("1:argument", "2:argument") — Sound velocity of meta-stable supercooled steam [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspWPH("1:argument", "2:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspWPS("1:argument", "2:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspWPT("1:argument", "2:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspWPTX("1:argument", "2:argument", "3:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspWSST("argument") — Sound velocity in steam at saturation line [m/sec] as function of temperature t "argument" [K].
  • wspWSTX("1:argument", "2:argument") — Sound velocity in double-phase area [m/sec] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspWSWT("argument") — Sound velocity in water at saturation line [m/sec] as function of temperature t "argument" [K].
  • wspXEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Vapor fraction at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspXEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Vapor fraction at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspXHS("1:argument", "2:argument") — Vapor fraction [-] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspXPH("1:argument", "2:argument") — Vapor fraction [-] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspXPS("1:argument", "2:argument") — Vapor fraction [-] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspXSTCP("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific isobaric heat capacity Cp "2:argument" [J/(kg·K)].
  • wspXSTCV("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific isochoric heat capacity Cv "2:argument" [J/(kg·K)].
  • wspXSTD("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], density r "2:argument" [kg/m3].
  • wspXSTDYNVIS("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], dynamic viscosity dv "2:argument" [Pa·sec].
  • wspXSTH("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific enthalpy h "2:argument" [J/kg].
  • wspXSTJOULETHOMPSON("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], Joule-Thomson coefficient jt "2:argument" [K/Pa].
  • wspXSTK("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], isoentropic exponent k "2:argument" [-].
  • wspXSTKINVIS("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], kinematic viscosity kv "2:argument" [m2/sec].
  • wspXSTPRANDTLE("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], Prandtl number pr "2:argument" [-].
  • wspXSTS("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific entropy s "2:argument" [J/(kg·K)].
  • wspXSTTHERMCOND("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], thermal conductivity coefficient tc "2:argument" [W/(m·K)].
  • wspXSTU("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific internal energy u "2:argument" [J/kg].
  • wspXSTV("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific volume v "2:argument" [m3/kg].
  • wspXSTW("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], speed of sound w "2:argument" [m/sec].
  • wspCP1PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 1 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCP2PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 2 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCP3PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 3 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCP3RT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 3 [J/(kg·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspCP5PT("1:argument", "2:argument") — Specific isobaric heat capacity in IF-97 region 5 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCPEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific isobaric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspCPEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific isobaric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspCPHS("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspCPMSPT("1:argument", "2:argument") — Specific isobaric heat capacity of meta-stable supercooled steam [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCPPH("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspCPPS("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspCPPT("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCPPTX("1:argument", "2:argument", "3:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspCPSST("argument") — Specific isobaric heat capacity of steam at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCPSTX("1:argument", "2:argument") — Specific isobaric heat capacity in double-phase area [J/(kg·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspCPSWT("argument") — Specific isobaric heat capacity of water at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCV1PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 1 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCV2PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 2 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCV3PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 3 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCV3RT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 3 [J/(kg·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspCV5PT("1:argument", "2:argument") — Specific isochoric heat capacity in IF-97 region 5 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCVDPSST("argument") — Specific isochoric heat capacity of steam at saturation line from the double-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCVDPSWT("argument") — Specific isochoric heat capacity of water at saturation line from the double-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCVEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific isochoric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspCVEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific isochoric heat capacity at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspCVHS("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspCVMSPT("1:argument", "2:argument") — Specific isochoric heat capacity of meta-stable supercooled steam [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCVPH("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspCVPS("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspCVPT("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspCVPTX("1:argument", "2:argument", "3:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspCVSST("argument") — Specific isochoric heat capacity of steam at saturation line from the one-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspCVSTX("1:argument", "2:argument") — Specific isochoric heat capacity in double-phase area [J/(kg·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspCVSWT("argument") — Specific isochoric heat capacity of water at saturation line from the one-phase region [J/(kg·K)] as function of temperature t "argument" [K].
  • wspD1PT("1:argument", "2:argument") — Density in IF-97 region 1 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspD2PT("1:argument", "2:argument") — Density in IF-97 region 2 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspD3PT("1:argument", "2:argument") — Density in IF-97 region 3 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspD5PT("1:argument", "2:argument") — Density in IF-97 region 5 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDCPT("1:argument", "2:argument") — Static dielectric constant of ordinary water substance [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDCRT("1:argument", "2:argument") — Static dielectric constant of ordinary water substance [-] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspDDDHPPH("1:argument", "2:argument") — Derivate of density on enthalpy with constant pressure of water/steam [kg·sec2/m5] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspDDDHPPT("1:argument", "2:argument") — Derivate of density on enthalpy with constant pressure of water/steam [kg·sec2/m5] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDDDHPPTX("1:argument", "2:argument", "3:argument") — Derivate of density on enthalpy with constant pressure of water/steam [kg·sec2/m5] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDDDHPSST("argument") — Derivate of density on enthalpy with constant pressure of steam at saturation line [kg·sec2/m5] as function of temperature t "argument" [K].
  • wspDDDHPSWT("argument") — Derivate of density on enthalpy with constant pressure of water at saturation line [kg·sec2/m5] as function of temperature t "argument" [K].
  • wspDDDPHPH("1:argument", "2:argument") — Derivate of density on pressure with constant enthalpy of water/steam [sec2/m2] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspDDDPHPT("1:argument", "2:argument") — Derivate of density on pressure with constant enthalpy of water/steam [sec2/m2] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDDDPHPTX("1:argument", "2:argument", "3:argument") — Derivate of density on pressure with constant enthalpy of water/steam [sec2/m2] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDDDPHSST("argument") — Derivate of density on pressure with constant enthalpy of steam at saturation line [sec2/m2] as function of temperature t "argument" [K].
  • wspDDDPHSWT("argument") — Derivate of density on pressure with constant enthalpy of water at saturation line [sec2/m2] as function of temperature t "argument" [K].
  • wspDPDTST("argument") — Derivative of saturation pressure on saturation temperature [Pa/K] as function of temperature t "argument" [K].
  • wspDPT("1:argument", "2:argument") — Density [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDPTX("1:argument", "2:argument", "3:argument") — Density [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDSST("argument") — Density of steam at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspDSTX("1:argument", "2:argument") — Density in double-phase area [kg/m3] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspDSWT("argument") — Density of water at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspDYNVISEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Dynamic viscosity at the end of expansion/compression process [Pa·sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspDYNVISEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Dynamic viscosity at the end of expansion/compression process [Pa·sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspDYNVISHS("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspDYNVISMSPT("1:argument", "2:argument") — Dynamic viscosity of meta-stable supercooled steam [Pa·sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDYNVISPH("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspDYNVISPS("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspDYNVISPT("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspDYNVISPTX("1:argument", "2:argument", "3:argument") — Dynamic viscosity [Pa·sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspDYNVISRT("1:argument", "2:argument") — Dynamic viscosity [Pa·sec] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspDYNVISSST("argument") — Dynamic viscosity of steam at saturation line [Pa·sec] as function of temperature t "argument" [K].
  • wspDYNVISSTX("1:argument", "2:argument") — Dynamic viscosity in double-phase area [Pa·sec] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspDYNVISSWT("argument") — Dynamic viscosity of water at saturation line [Pa·sec] as function of temperature t "argument" [K].
  • wspgADDGASM("1:argument", "2:argument", "3:argument") — Addition of one gas to another as function of identificator of target gas [-], identificator of added gas "1:argument" [-], added gas mass "2:argument" [-].
  • wspgADDGASV("1:argument", "2:argument", "3:argument") — Addition of one gas to another as function of identificator of target gas [-], identificator of added gas "1:argument" [-], added gas volume "2:argument" [-].
  • wspgCPGST("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgCPIDT("1:argument", "2:argument") — Specific isobaric heat capacity [J/(kg·K)] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgCVGST("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgCVIDT("1:argument", "2:argument") — Specific isochoric heat capacity [J/(kg·K)] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgDELETEGASES("argument") — Deleting of all user-defined gases.
  • wspgDELETEGASID("argument") — Deleting of early created gas as function of gas identificator [-].
  • wspGETABSOLUTEGASCONSTANT("argument") — Absolute gas constant [J/(mole·K)].
  • wspGETCHECKRANGEMODE("argument") — Mode of checking the range of functions arguments.
  • wspGETDELTAPRESSURE("argument") — Maximum difference between pressure values at estimation of the area 3 parameters [Pa].
  • wspGETDELTATS("argument") — Maximum difference between saturation temperature and input temperature for function wspWATERSTATEAREA [K].
  • wspGETINITSTEAMDENSITY("argument") — Initial value for density of steam in IF-97 region 3 [kg/m3].
  • wspGETINITWATERDENSITY("argument") — Initial value for density of water in IF-97 region 3 [kg/m3].
  • wspGETLASTERROR("argument") — Last error code.
  • wspGETLASTERRORDESCRIPTION("argument") — Last error description.
  • wspGETLASTERRORDESCRIPTIONW("argument") — Last error description.
  • wspGETMAXITERATION("argument") — Maximum iterations count for Newton method.
  • wspGETTOLERANCE("argument") — Relative precision in the WaterSteamPro functions [-].
  • wspGETTOLERANCEMODE("argument") — Mode of management of make function results more precise.
  • wspGETWSPVERSION("argument") — Internal version of the WaterSteamPro.
  • wspgGASESCOUNT("argument") — Available gases count.
  • wspgGCGS("argument") — Specific gas constant [J/(kg·K)] as function of gas specification "argument" [-].
  • wspgGCID("argument") — Specific gas constant [J/(kg·K)] as function of gas identificator "argument" [-].
  • wspgGETCALCDISSMODE("argument") — Mode of calculating dissociation while calculate gases mixtures.
  • wspgHGST("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgHIDT("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgIDNAME("argument") — Gas identificator as function of existing gas name [-].
  • wspgMFGSGS("1:argument", "2:argument") — Mass fraction (MF) of gas as function of primary gas specification [-], gas specification looked for "1:argument" [-].
  • wspgMFIDID("1:argument", "2:argument") — Mass fraction (MF) of gas as function of primary gas identificator [-], gas identificator looked for "1:argument" [-].
  • wspgMMGS("argument") — Molar mass [kg/mole] as function of gas specification "argument" [-].
  • wspgMMID("argument") — Molar mass [kg/mole] as function of gas identificator "argument" [-].
  • wspgNEWID("argument") — New gas identificator.
  • wspgNEWIDGS("argument") — New gas identificator as function of gas specification [-].
  • wspgNEWIDNAME("argument") — Gas identificator as function of new gas name [-].
  • wspgPGSTS("1:argument", "2:argument", "3:argument") — Pressure [Pa] as function of gas specification "1:argument" [-], temperature t "2:argument" [K], specific entropy s "3:argument" [J/(kg·K)].
  • wspgPIDTS("1:argument", "2:argument", "3:argument") — Pressure [Pa] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K], specific entropy s "3:argument" [J/(kg·K)].
  • wspgSETCALCDISSMODE("argument") — Set and return a mode of calculating dissociation while calculate gases mixtures as function of mode [-].
  • wspgSGSPT("1:argument", "2:argument", "3:argument") — Specific entropy [J/(kg·K)] as function of gas specification "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgSGST("1:argument", "2:argument") — Specific entropy at pressure p0 = 100 kPa [J/(kg·K)] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgSIDPT("1:argument", "2:argument", "3:argument") — Specific entropy [J/(kg·K)] as function of gas identificator "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgSIDT("1:argument", "2:argument") — Specific entropy at pressure p0 = 100 kPa [J/(kg·K)] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgTGSH("1:argument", "2:argument") — Temperature [K] as function of gas specification "1:argument" [-], specific enthalpy h "2:argument" [J/kg].
  • wspgTGSPS("1:argument", "2:argument", "3:argument") — Temperature [K] as function of gas specification "1:argument" [-], pressure p "2:argument" [Pa], specific entropy s "3:argument" [J/(kg·K)].
  • wspgTGSS("1:argument", "2:argument") — Temperature at pressure p0 = 100 kPa [K] as function of gas specification "1:argument" [-], specific entropy s "2:argument" [J/(kg·K)].
  • wspgTIDH("1:argument", "2:argument") — Temperature [K] as function of gas identificator "1:argument" [-], specific enthalpy h "2:argument" [J/kg].
  • wspgTIDPS("1:argument", "2:argument", "3:argument") — Temperature [K] as function of gas identificator "1:argument" [-], pressure p "2:argument" [Pa], specific entropy s "3:argument" [J/(kg·K)].
  • wspgTIDS("1:argument", "2:argument") — Temperature at pressure p0 = 100 kPa [K] as function of gas identificator "1:argument" [-], specific entropy s "2:argument" [J/(kg·K)].
  • wspgUGST("1:argument", "2:argument") — Specific internal energy [J/kg] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgUIDT("1:argument", "2:argument") — Specific internal energy [J/kg] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspgVFGSGS("1:argument", "2:argument") — Volume fraction (VF) of gas as function of primary gas specification [-], gas specification looked for "1:argument" [-].
  • wspgVFIDID("1:argument", "2:argument") — Volume fraction (VF) of gas as function of primary gas identificator [-], gas identificator looked for "1:argument" [-].
  • wspgVGSPT("1:argument", "2:argument", "3:argument") — Specific volume [m3/kg] as function of gas specification "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgVGST("1:argument", "2:argument") — Specific volume at pressure p0 = 100 kPa [m3/kg] as function of gas specification "1:argument" [-], temperature t "2:argument" [K].
  • wspgVIDPT("1:argument", "2:argument", "3:argument") — Specific volume [m3/kg] as function of gas identificator "1:argument" [-], pressure p "2:argument" [Pa], temperature t "3:argument" [K].
  • wspgVIDT("1:argument", "2:argument") — Specific volume at pressure p0 = 100 kPa [m3/kg] as function of gas identificator "1:argument" [-], temperature t "2:argument" [K].
  • wspH1PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 1 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspH2B2CP("argument") — Specific enthalpy at line between areas 2b and 2c [J/kg] as function of pressure p "argument" [Pa].
  • wspH2PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 2 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspH3PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 3 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspH3RT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 3 [J/kg] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspH5PT("1:argument", "2:argument") — Specific enthalpy in IF-97 region 5 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspHB13S("argument") — Specific enthalpy at boundary line between areas 1 and 3 [J/kg] as function of specific entropy s "argument" [J/(kg·K)].
  • wspHEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific enthalpy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspHEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific enthalpy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspHMSPT("1:argument", "2:argument") — Specific enthalpy of meta-stable supercooled steam [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspHPS("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspHPT("1:argument", "2:argument") — Specific enthalpy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspHPTX("1:argument", "2:argument", "3:argument") — Specific enthalpy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspHSST("argument") — Specific enthalpy of steam at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspHSTX("1:argument", "2:argument") — Specific enthalpy in double-phase area [J/kg] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspHSWT("argument") — Specific enthalpy of water at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspJOULETHOMPSON1PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 1 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSON2PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 2 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSON3PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 3 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSON3RT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 3 [K/Pa] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspJOULETHOMPSON5PT("1:argument", "2:argument") — Joule-Thomson coefficient in IF-97 region 5 [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSONEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Joule-Thomson coefficient at the end of expansion/compression process [K/Pa] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspJOULETHOMPSONEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Joule-Thomson coefficient at the end of expansion/compression process [K/Pa] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspJOULETHOMPSONHS("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspJOULETHOMPSONMSPT("1:argument", "2:argument") — Joule-Thomson coefficient of meta-stable supercooled steam [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSONPH("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspJOULETHOMPSONPS("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspJOULETHOMPSONPT("1:argument", "2:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspJOULETHOMPSONPTX("1:argument", "2:argument", "3:argument") — Joule-Thomson coefficient [K/Pa] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspJOULETHOMPSONSST("argument") — Joule-Thomson coefficient of steam at saturation line [K/Pa] as function of temperature t "argument" [K].
  • wspJOULETHOMPSONSTX("1:argument", "2:argument") — Joule-Thomson coefficient in double-phase area [K/Pa] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspJOULETHOMPSONSWT("argument") — Joule-Thomson coefficient of water at saturation line [K/Pa] as function of temperature t "argument" [K].
  • wspKEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Isoentropic exponent at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspKEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Isoentropic exponent [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspKHS("1:argument", "2:argument") — Isoentropic exponent [-] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspKINVISEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Kinematic viscosity at the end of expansion/compression process [m2/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspKINVISEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Kinematic viscosity at the end of expansion/compression process [m2/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspKINVISHS("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspKINVISMSPT("1:argument", "2:argument") — Kinematic viscosity of meta-stable supercooled steam [m2/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKINVISPH("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspKINVISPS("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspKINVISPT("1:argument", "2:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKINVISPTX("1:argument", "2:argument", "3:argument") — Kinematic viscosity [m2/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspKINVISSST("argument") — Kinematic viscosity of steam at saturation line [m2/sec] as function of temperature t "argument" [K].
  • wspKINVISSTX("1:argument", "2:argument") — Kinematic viscosity in double-phase area [m2/sec] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspKINVISSWT("argument") — Kinematic viscosity of water at saturation line [m2/sec] as function of temperature t "argument" [K].
  • wspKMSPT("1:argument", "2:argument") — Isoentropic exponent of meta-stable supercooled steam [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKPH("1:argument", "2:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspKPS("1:argument", "2:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspKPT("1:argument", "2:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspKPTX("1:argument", "2:argument", "3:argument") — Isoentropic exponent [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspKSST("argument") — Isoentropic exponent of steam at saturation line [-] as function of temperature t "argument" [K].
  • wspKSTX("1:argument", "2:argument") — Isoentropic exponent in double-phase area [-] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspKSWT("argument") — Isoentropic exponent of water at saturation line [-] as function of temperature t "argument" [K].
  • wspLOCALREGISTRATIONEXA("1:argument", "2:argument") — Process registration of the WaterSteamPro as function of registration name [-], registration data "1:argument" [-].
  • wspLOCALREGISTRATIONEXW("1:argument", "2:argument") — Process registration of the WaterSteamPro as function of registration name [-], registration data "1:argument" [-].
  • wspP1HS("1:argument", "2:argument") — Pressure in IF-97 region 1 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspP23T("argument") — Pressure at line between areas 2 and 3 [Pa] as function of temperature t "argument" [K].
  • wspP2B2CH("argument") — Pressure at line between areas 2b and 2c [Pa] as function of specific enthalpy h "argument" [J/kg].
  • wspP2HS("1:argument", "2:argument") — Pressure in IF-97 region 2 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspP3HS("1:argument", "2:argument") — Pressure in IF-97 region 3 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspP3RT("1:argument", "2:argument") — Pressure in IF-97 region 3 [Pa] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspP5HS("1:argument", "2:argument") — Pressure in IF-97 region 5 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPB23HS("1:argument", "2:argument") — Pressure at boundary line between areas 2 and 3 [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPHASESTATEPT("1:argument", "2:argument") — Area of phase state as function of pressure p [Pa], temperature t "1:argument" [K].
  • wspPHS("1:argument", "2:argument") — Pressure [Pa] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPKWPT("1:argument", "2:argument") — Negative logarithm (base 10) of the ionization constant of water [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspPKWRT("1:argument", "2:argument") — Negative logarithm (10 base) of the ionization constant of water [-] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspPMELTIT("argument") — Pressure at melting line of ice I [Pa] as function of temperature t "argument" [K].
  • wspPRANDTLEEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Prandtl number at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspPRANDTLEEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Prandtl number at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspPRANDTLEHS("1:argument", "2:argument") — Prandtl number [-] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspPRANDTLEMSPT("1:argument", "2:argument") — Prandtl number of meta-stable supercooled steam [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspPRANDTLEPH("1:argument", "2:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspPRANDTLEPS("1:argument", "2:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspPRANDTLEPT("1:argument", "2:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspPRANDTLEPTX("1:argument", "2:argument", "3:argument") — Prandtl number [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspPRANDTLESST("argument") — Prandtl number of steam at saturation line [-] as function of temperature t "argument" [K].
  • wspPRANDTLESTX("1:argument", "2:argument") — Prandtl number in double-phase area [-] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspPRANDTLESWT("argument") — Prandtl number of water at saturation line [-] as function of temperature t "argument" [K].
  • wspPST("argument") — Pressure at saturation line [Pa] as function of temperature t "argument" [K].
  • wspPSUBT("argument") — Pressure at sublimation line [Pa] as function of temperature t "argument" [K].
  • wspR3PT("1:argument", "2:argument") — Density in IF-97 region 3 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspR3PTR0("1:argument", "2:argument", "3:argument") — Density in IF-97 region 3 [kg/m3] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], initial density r0 "3:argument" [kg/m3].
  • wspRIPTL("1:argument", "2:argument", "3:argument") — Refractive index [-] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], wave length wavelength "3:argument" [m].
  • wspRIRTL("1:argument", "2:argument", "3:argument") — Refractive index [-] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K], wave length wavelength "3:argument" [m].
  • wspROUGHHSSS("argument") — Specific enthalpy of steam at saturation line [J/kg] as function of specific entropy s "argument" [J/(kg·K)].
  • wspROUGHHSWS("argument") — Specific enthalpy of water at saturation line [J/kg] as function of specific entropy s "argument" [J/(kg·K)].
  • wspROUGHRSST("argument") — Rough value of density of steam at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspROUGHRSWT("argument") — Rough value of density of water at saturation line [kg/m3] as function of temperature t "argument" [K].
  • wspRST("argument") — Specific evaporation heat [J/kg] as function of temperature t "argument" [K].
  • wspS1PT("1:argument", "2:argument") — Specific entropy in IF-97 region 1 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspS2PT("1:argument", "2:argument") — Specific entropy in IF-97 region 2 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspS3PT("1:argument", "2:argument") — Specific entropy in IF-97 region 3 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspS3RT("1:argument", "2:argument") — Specific entropy in IF-97 region 3 [J/(kg·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspS5PT("1:argument", "2:argument") — Specific entropy in IF-97 region 5 [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspSETCHECKRANGEMODE("argument") — Set and return a mode of checking the range of functions arguments as function of mode [-].
  • wspSETDELTAPRESSURE("argument") — Set and return maximum difference between pressure values at estimation of the area 3 parameters [Pa] as function of delta pressure delta "argument" [Pa].
  • wspSETDELTATS("argument") — Set and return maximum difference between saturation temperature and input temperature for function wspWATERSTATEAREA [K] as function of temperature delta "argument" [_K].
  • wspSETINITSTEAMDENSITY("argument") — Set and return the initial value for density of steam in IF-97 region 3 [kg/m3] as function of density r "argument" [kg/m3].
  • wspSETINITWATERDENSITY("argument") — Set and return initial value for density of water in IF-97 region 3 [kg/m3] as function of density r "argument" [kg/m3].
  • wspSETLASTERROR("argument") — Set and return a last error code as function of error code [-].
  • wspSETMAXITERATION("argument") — Set and return maximum iterations count for Newton method as function of maximum iteration [-].
  • wspSETTOLERANCE("argument") — Set and return relative precision in the WaterSteamPro functions [-] as function of tolerance "argument" [_-].
  • wspSETTOLERANCEMODE("argument") — Set and return a mode of management of make function results more precise as function of mode [-].
  • wspSEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific entropy at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspSEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific entropy at the end of expansion/compression process [J/(kg·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspSMSPT("1:argument", "2:argument") — Specific entropy of meta-stable supercooled steam [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspSPH("1:argument", "2:argument") — Specific entropy [J/(kg·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspSPT("1:argument", "2:argument") — Specific entropy [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspSPTX("1:argument", "2:argument", "3:argument") — Specific entropy [J/(kg·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspSSST("argument") — Specific entropy of steam at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspSSTX("1:argument", "2:argument") — Specific entropy in double-phase area [J/(kg·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspSSWT("argument") — Specific entropy of water at saturation line [J/(kg·K)] as function of temperature t "argument" [K].
  • wspSURFTENT("argument") — Surface tension [N/m] as function of temperature t "argument" [K].
  • wspT1HS("1:argument", "2:argument") — Temperature in IF-97 region 1 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT1PH("1:argument", "2:argument") — Temperature in IF-97 region 1 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT1PS("1:argument", "2:argument") — Temperature in IF-97 region 1 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT23P("argument") — Temperature at line between areas 2 and 3 [K] as function of pressure p "argument" [Pa].
  • wspT2APH("1:argument", "2:argument") — Temperature in IF-97 region 2a [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2APS("1:argument", "2:argument") — Temperature in IF-97 region 2a [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2BPH("1:argument", "2:argument") — Temperature in IF-97 region 2b [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2BPS("1:argument", "2:argument") — Temperature in IF-97 region 2b [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2CPH("1:argument", "2:argument") — Temperature in IF-97 region 2c [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2CPS("1:argument", "2:argument") — Temperature in IF-97 region 2c [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2HS("1:argument", "2:argument") — Temperature in IF-97 region 2 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT2PH("1:argument", "2:argument") — Temperature in IF-97 region 2 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT2PS("1:argument", "2:argument") — Temperature in IF-97 region 2 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT3HS("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT3PH("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT3PS("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspT3RH("1:argument", "2:argument") — Temperature in IF-97 region 3 [K] as function of density r "1:argument" [kg/m3], specific enthalpy h "2:argument" [J/kg].
  • wspT5HS("1:argument", "2:argument") — Temperature in IF-97 region 5 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspT5PH("1:argument", "2:argument") — Temperature in IF-97 region 5 [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspT5PS("1:argument", "2:argument") — Temperature in IF-97 region 5 [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspTB23HS("1:argument", "2:argument") — Temperature at boundary line between areas 2 and 3 [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Temperature at the end of expansion/compression process [K] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspTEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Temperature at the end of expansion/compression process [K] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspTHERMCONDEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Thermal conductivity coefficient at the end of expansion/compression process [W/(m·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspTHERMCONDEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Thermal conductivity coefficient at the end of expansion/compression process [W/(m·K)] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspTHERMCONDHS("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTHERMCONDMSPT("1:argument", "2:argument") — Thermal conductivity coefficient of meta-stable supercooled steam [W/(m·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspTHERMCONDPH("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspTHERMCONDPS("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspTHERMCONDPT("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspTHERMCONDPTX("1:argument", "2:argument", "3:argument") — Thermal conductivity coefficient [W/(m·K)] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspTHERMCONDRT("1:argument", "2:argument") — Thermal conductivity coefficient [W/(m·K)] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspTHERMCONDSST("argument") — Thermal conductivity coefficient of steam at saturation line [W/(m·K)] as function of temperature t "argument" [K].
  • wspTHERMCONDSTX("1:argument", "2:argument") — Thermal conductivity coefficient in double-phase area [W/(m·K)] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspTHERMCONDSWT("argument") — Thermal conductivity coefficient of water at saturation line [W/(m·K)] as function of temperature t "argument" [K].
  • wspTHS("1:argument", "2:argument") — Temperature [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTPH("1:argument", "2:argument") — Temperature [K] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspTPS("1:argument", "2:argument") — Temperature [K] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspTSHS("1:argument", "2:argument") — Temperature at saturation line [K] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspTSP("argument") — Temperature at saturation line [K] as function of pressure p "argument" [Pa].
  • wspU1PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 1 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspU2PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 2 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspU3PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 3 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspU3RT("1:argument", "2:argument") — Specific internal energy in IF-97 region 3 [J/kg] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspU5PT("1:argument", "2:argument") — Specific internal energy in IF-97 region 5 [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspUEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific internal energy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspUEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific internal energy at the end of expansion/compression process [J/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspUHS("1:argument", "2:argument") — Specific internal energy [J/kg] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspUMSPT("1:argument", "2:argument") — Specific internal energy of meta-stable supercooled steam [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspUPH("1:argument", "2:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspUPS("1:argument", "2:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspUPT("1:argument", "2:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspUPTX("1:argument", "2:argument", "3:argument") — Specific internal energy [J/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspUSST("argument") — Specific internal energy of steam at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspUSTX("1:argument", "2:argument") — Specific internal energy in double-phase area [J/kg] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspUSWT("argument") — Specific internal energy of water at saturation line [J/kg] as function of temperature t "argument" [K].
  • wspV1PT("1:argument", "2:argument") — Specific volume in IF-97 region 1 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspV2PT("1:argument", "2:argument") — Specific volume in IF-97 region 2 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspV3HS("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspV3PH("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspV3PS("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspV3PT("1:argument", "2:argument") — Specific volume in IF-97 region 3 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspV5PT("1:argument", "2:argument") — Specific volume in IF-97 region 5 [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspVEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Specific volume at the end of expansion/compression process [m3/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspVEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Specific volume at the end of expansion/compression process [m3/kg] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspVHS("1:argument", "2:argument") — Specific volume [m3/kg] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspVMSPT("1:argument", "2:argument") — Specific volume of meta-stable supercooled steam [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspVPH("1:argument", "2:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspVPS("1:argument", "2:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspVPT("1:argument", "2:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspVPTX("1:argument", "2:argument", "3:argument") — Specific volume [m3/kg] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspVSST("argument") — Specific volume of steam at saturation line [m3/kg] as function of temperature t "argument" [K].
  • wspVSTX("1:argument", "2:argument") — Specific volume in double-phase area [m3/kg] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspVSWT("argument") — Specific volume of water at saturation line [m3/kg] as function of temperature t "argument" [K].
  • wspW1PT("1:argument", "2:argument") — Sound velocity in IF-97 region 1 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspW2PT("1:argument", "2:argument") — Sound velocity in IF-97 region 2 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspW3PT("1:argument", "2:argument") — Sound velocity in IF-97 region 3 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspW3RT("1:argument", "2:argument") — Sound velocity in IF-97 region 3 [m/sec] as function of density r "1:argument" [kg/m3], temperature t "2:argument" [K].
  • wspW5PT("1:argument", "2:argument") — Sound velocity in IF-97 region 5 [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspWATERSTATEAREA("1:argument", "2:argument") — IF-97 region as function of pressure p [Pa], temperature t "1:argument" [K].
  • wspWATERSTATEAREA2("1:argument", "2:argument") — IF-97 region (version 2) as function of pressure p [Pa], temperature t "1:argument" [K].
  • wspWATERSTATEAREAHS("1:argument", "2:argument") — IF-97 region as function of specific enthalpy h [J/kg], specific entropy s "1:argument" [J/(kg·K)].
  • wspWATERSTATEAREAPH("1:argument", "2:argument") — IF-97 region as function of pressure p [Pa], specific enthalpy h "1:argument" [J/kg].
  • wspWATERSTATEAREAPS("1:argument", "2:argument") — IF-97 region as function of pressure p [Pa], specific entropy s "1:argument" [J/(kg·K)].
  • wspWEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Sound velocity at the end of expansion/compression process [m/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspWEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Sound velocity at the end of expansion/compression process [m/sec] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspWHS("1:argument", "2:argument") — Speed of sound [m/sec] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspWMSPT("1:argument", "2:argument") — Sound velocity of meta-stable supercooled steam [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspWPH("1:argument", "2:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspWPS("1:argument", "2:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspWPT("1:argument", "2:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K].
  • wspWPTX("1:argument", "2:argument", "3:argument") — Speed of sound [m/sec] as function of pressure p "1:argument" [Pa], temperature t "2:argument" [K], vapor fraction x "3:argument" [-].
  • wspWSST("argument") — Sound velocity in steam at saturation line [m/sec] as function of temperature t "argument" [K].
  • wspWSTX("1:argument", "2:argument") — Sound velocity in double-phase area [m/sec] as function of temperature t "1:argument" [K], vapor fraction x "2:argument" [-].
  • wspWSWT("argument") — Sound velocity in water at saturation line [m/sec] as function of temperature t "argument" [K].
  • wspXEXPANSIONPTPEFF("1:argument", "2:argument", "3:argument", "4:argument") — Vapor fraction at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], pressure at final point p1 "3:argument" [Pa], internal efficiency of process eff "4:argument" [-].
  • wspXEXPANSIONPTXPEFF("1:argument", "2:argument", "3:argument", "4:argument", "5:argument") — Vapor fraction at the end of expansion/compression process [-] as function of pressure at initial point p0 "1:argument" [Pa], temperature at initial point t0 "2:argument" [K], vapor fraction at initial point x0 "3:argument" [-], pressure at final point p1 "4:argument" [Pa], internal efficiency of process eff "5:argument" [-].
  • wspXHS("1:argument", "2:argument") — Vapor fraction [-] as function of specific enthalpy h "1:argument" [J/kg], specific entropy s "2:argument" [J/(kg·K)].
  • wspXPH("1:argument", "2:argument") — Vapor fraction [-] as function of pressure p "1:argument" [Pa], specific enthalpy h "2:argument" [J/kg].
  • wspXPS("1:argument", "2:argument") — Vapor fraction [-] as function of pressure p "1:argument" [Pa], specific entropy s "2:argument" [J/(kg·K)].
  • wspXSTCP("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific isobaric heat capacity Cp "2:argument" [J/(kg·K)].
  • wspXSTCV("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific isochoric heat capacity Cv "2:argument" [J/(kg·K)].
  • wspXSTD("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], density r "2:argument" [kg/m3].
  • wspXSTDYNVIS("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], dynamic viscosity dv "2:argument" [Pa·sec].
  • wspXSTH("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific enthalpy h "2:argument" [J/kg].
  • wspXSTJOULETHOMPSON("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], Joule-Thomson coefficient jt "2:argument" [K/Pa].
  • wspXSTK("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], isoentropic exponent k "2:argument" [-].
  • wspXSTKINVIS("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], kinematic viscosity kv "2:argument" [m2/sec].
  • wspXSTPRANDTLE("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], Prandtl number pr "2:argument" [-].
  • wspXSTS("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific entropy s "2:argument" [J/(kg·K)].
  • wspXSTTHERMCOND("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], thermal conductivity coefficient tc "2:argument" [W/(m·K)].
  • wspXSTU("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific internal energy u "2:argument" [J/kg].
  • wspXSTV("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], specific volume v "2:argument" [m3/kg].
  • wspXSTW("1:argument", "2:argument") — Vapor fraction [-] as function of temperature t "1:argument" [K], speed of sound w "2:argument" [m/sec].