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].