List of WaterSteamPro functions for versions:

Version 5.6

  1. Properties calculation result (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: pressure p [Pa], temperature t [K]:

    wspVUSHCVWDERPTPT(p, t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

  2. Properties calculation result in area 1 (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: pressure p [Pa], temperature t [K]:

    wspVUSHCVWDERPT1PT(p, t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

  3. Properties calculation result in area 2 (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: pressure p [Pa], temperature t [K]:

    wspVUSHCVWDERPT2PT(p, t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

  4. Properties calculation result in area 3 (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: density r [kg/m3], temperature t [K]:

    wspVUSHCVWDERPT3RT(r, t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

  5. Properties calculation result in area 3 (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: pressure p [Pa], temperature t [K]:

    wspVUSHCVWDERPT3PT(p, t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

  6. Properties calculation result in area 5 (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: pressure p [Pa], temperature t [K]:

    wspVUSHCVWDERPT5PT(p, t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

  7. Derivative of saturation pressure on saturation temperature [Pa/K] as function of: temperature t [K]:

    wspDPDTST(t)

  8. Specific isochoric heat capacity (Cv) of steam at saturation line from the double-phase region [J/(kg·K)] as function of: temperature t [K]:

    wspCVDPSST(t)

  9. Specific isochoric heat capacity (Cv) of water at saturation line from the double-phase region [Ac/(ea·K)] as function of: nledldrnodr t [K]:

    wspCVDPSWT(t)

  10. Properties calculation result for water at saturation line (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: temperature t [K]:

    wspVUSHCVWDERPTSWT(t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

  11. Properties calculation result for steam at saturation line (V, U, S, H, CV, W, DVDPt, DUDPt, DSDPt, DHDPt, DVDTp, DUDTp, DSDTp, DHDTp) as function of: temperature t [K]:

    wspVUSHCVWDERPTSST(t, *V, *U, *S, *H, *CV, *W, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

Version 5.5

  1. Specific volume of meta-stable supercooled steam [m3/kg] as function of: pressure p [Pa], temperature t [K]:

    wspVMSPT(p, t)

  2. Specific internal energy of meta-stable supercooled steam [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspUMSPT(p, t)

  3. Specific entropy of meta-stable supercooled steam [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspSMSPT(p, t)

  4. Specific enthalpy of meta-stable supercooled steam [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspHMSPT(p, t)

  5. Specific heat capacity at constant pressure (Cp) of meta-stable supercooled steam [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCPMSPT(p, t)

  6. Specific heat capacity at constant volume (Cv) of meta-stable supercooled steam [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCVMSPT(p, t)

  7. Sound velocity of meta-stable supercooled steam [m/sec] as function of: pressure p [Pa], temperature t [K]:

    wspWMSPT(p, t)

  8. Thermal conduction of meta-stable supercooled steam [W/(m·K)] as function of: pressure p [Pa], temperature t [K]:

    wspTHERMCONDMSPT(p, t)

  9. Dynamic viscosity of meta-stable supercooled steam [Pa·sec] as function of: pressure p [Pa], temperature t [K]:

    wspDYNVISMSPT(p, t)

  10. Prandtl number of meta-stable supercooled steam as function of: pressure p [Pa], temperature t [K]:

    wspPRANDTLEMSPT(p, t)

  11. Kinematic viscosity of meta-stable supercooled steam [m2/sec] as function of: pressure p [Pa], temperature t [K]:

    wspKINVISMSPT(p, t)

  12. Isoentropic exponent of meta-stable supercooled steam as function of: pressure p [Pa], temperature t [K]:

    wspKMSPT(p, t)

  13. Joule-Thompson coefficient of meta-stable supercooled steam [K/Pa] as function of: pressure p [Pa], temperature t [K]:

    wspJOULETHOMPSONMSPT(p, t)

Version 5.4

  1. Temperature [K] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspTEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  2. Specific volume [m3/kg] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspVEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  3. Specific internal energy [J/kg] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspUEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  4. Specific enthalpy [J/kg] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspHEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  5. Specific entropy [J/(kg·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspSEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  6. Specific heat capacity at constant pressure (Cp) [J/(kg·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspCPEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  7. Specific heat capacity at constant volume (Cv) [J/(kg·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspCVEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  8. Sound velocity [m/sec] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspWEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  9. Thermal conduction [W/(m·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspTHERMCONDEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  10. Kinematic viscosity [m2/sec] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspKINVISEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  11. Dynamic viscocity [Pa·sec] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspDYNVISEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  12. Prandtl number as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspPRANDTLEEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  13. Isoentropic coefficient as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspKEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  14. Joule-Thompson coefficient [K/Pa] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspJOULETHOMPSONEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  15. Degree of dryness as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], degree of dryness in initial point x0 [], pressure in final point p1 [Pa], internal efficiency eff []:

    wspXEXPANSIONPTXPEFF(p0, t0, x0, p1, eff)

  16. Degree of dryness as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspXEXPANSIONPTPEFF(p0, t0, p1, eff)

Version 5.3

  1. Temperature [K] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspTEXPANSIONPTPEFF(p0, t0, p1, eff)

  2. Specific volume [m3/kg] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspVEXPANSIONPTPEFF(p0, t0, p1, eff)

  3. Specific internal energy [J/kg] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspUEXPANSIONPTPEFF(p0, t0, p1, eff)

  4. Specific enthalpy [J/kg] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspHEXPANSIONPTPEFF(p0, t0, p1, eff)

  5. Specific entropy [J/(kg·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspSEXPANSIONPTPEFF(p0, t0, p1, eff)

  6. Specific heat capacity at constant pressure (Cp) [J/(kg·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspCPEXPANSIONPTPEFF(p0, t0, p1, eff)

  7. Specific heat capacity at constant volume (Cv) [J/(kg·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspCVEXPANSIONPTPEFF(p0, t0, p1, eff)

  8. Sound velocity [m/sec] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspWEXPANSIONPTPEFF(p0, t0, p1, eff)

  9. Thermal conduction [W/(m·K)] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspTHERMCONDEXPANSIONPTPEFF(p0, t0, p1, eff)

  10. Kinematic viscosity [m2/sec] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspKINVISEXPANSIONPTPEFF(p0, t0, p1, eff)

  11. Dynamic viscocity [Pa·sec] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspDYNVISEXPANSIONPTPEFF(p0, t0, p1, eff)

  12. Prandtl number as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspPRANDTLEEXPANSIONPTPEFF(p0, t0, p1, eff)

  13. Isoentropic coefficient as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspKEXPANSIONPTPEFF(p0, t0, p1, eff)

  14. Joule-Thompson coefficient [K/Pa] as function of: pressure in initial point p0 [Pa], temperature in initial point t0 [K], pressure in final point p1 [Pa], internal efficiency eff []:

    wspJOULETHOMPSONEXPANSIONPTPEFF(p0, t0, p1, eff)

Version 5.2

  1. Joule-Thompson coefficient [K/Pa] as function of: pressure p [Pa], temperature t [K]:

    wspJOULETHOMPSONPT(p, t)

  2. Joule-Thompson coefficient [K/Pa] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspJOULETHOMPSONPTX(p, t, x)

  3. Temperature [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspTPH(p, h)

  4. Temperature [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspTPS(p, s)

  5. Specific internal energy [J/kg] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspUPH(p, h)

  6. Specific volume [m3/kg] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspVPH(p, h)

  7. Specific entropy [J/(kg·K)] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspSPH(p, h)

  8. Specific heat capacity at constant pressure (Cp) [J/(kg·K)] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspCPPH(p, h)

  9. Specific heat capacity at constant volume (Cv) [J/(kg·K)] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspCVPH(p, h)

  10. Sound velocity [m/sec] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspWPH(p, h)

  11. Dynamic viscosity [Pa·sec] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspDYNVISPH(p, h)

  12. Kinematic viscosity [m2/sec] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspKINVISPH(p, h)

  13. Prandtl number as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspPRANDTLEPH(p, h)

  14. Thermal conduction [W/(m·K)] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspTHERMCONDPH(p, h)

  15. Isoentropic exponent as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspKPH(p, h)

  16. Joule-Thompson coefficient [K/Pa] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspJOULETHOMPSONPH(p, h)

  17. Specific internal energy [J/kg] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspUPS(p, s)

  18. Specific volume [m3/kg] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspVPS(p, s)

  19. Specific enthalpy [J/kg] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspHPS(p, s)

  20. Specific heat capacity at constant pressure (Cp) [J/(kg·K)] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspCPPS(p, s)

  21. Specific heat capacity at constant volume (Cv) [J/(kg·K)] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspCVPS(p, s)

  22. Sound velocity [m/sec] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspWPS(p, s)

  23. Dynamic viscosity [Pa·sec] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspDYNVISPS(p, s)

  24. Kinematic viscosity [m2/sec] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspKINVISPS(p, s)

  25. Prandtl number as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspPRANDTLEPS(p, s)

  26. Isoentropic exponent as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspKPS(p, s)

  27. Thermal conduction [W/(m·K)] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspTHERMCONDPS(p, s)

  28. Joule-Thompson coefficient [K/Pa] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspJOULETHOMPSONPS(p, s)

  29. Joule-Thompson coefficient in area 1 [K/Pa] as function of: pressure p [Pa], temperature t [K]:

    wspJOULETHOMPSON1PT(p, t)

  30. Joule-Thompson coefficient in area 2 [K/Pa] as function of: pressure p [Pa], temperature t [K]:

    wspJOULETHOMPSON2PT(p, t)

  31. Joule-Thompson coefficient in area 3 [K/Pa] as function of: density r [kg/m3], temperature t [K]:

    wspJOULETHOMPSON3RT(r, t)

  32. Joule-Thompson coefficient in area 3 [K/Pa] as function of: pressure p [Pa], temperature t [K]:

    wspJOULETHOMPSON3PT(p, t)

  33. Joule-Thompson coefficient in area 5 [K/Pa] as function of: pressure p [Pa], temperature t [K]:

    wspJOULETHOMPSON5PT(p, t)

  34. Temperature in area 1 [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspT1PH(p, h)

  35. Temperature in area 1 [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspT1PS(p, s)

  36. Temperature in area 2a [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspT2APH(p, h)

  37. Temperature in area 2a [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspT2APS(p, s)

  38. Temperature in area 2b [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspT2BPH(p, h)

  39. Temperature in area 2b [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspT2BPS(p, s)

  40. Temperature in area 2c [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspT2CPH(p, h)

  41. Temperature in area 2c [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspT2CPS(p, s)

  42. Temperature in area 2 [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspT2PH(p, h)

  43. Temperature in area 2 [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspT2PS(p, s)

  44. Temperature in area 3 [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspT3PH(p, h)

  45. Temperature in area 3 [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspT3PS(p, s)

  46. Temperature in area 5 [K] as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspT5PH(p, h)

  47. Temperature in area 5 [K] as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspT5PS(p, s)

  48. Pressure at line between areas 2b and 2c [Pa] as function of: specific enthalpy h [J/kg]:

    wspP2B2CH(h)

  49. Specific enthalpy at line between areas 2b and 2c [J/kg] as function of: pressure p [Pa]:

    wspH2B2CP(p)

  50. Water State Area as function of: pressure p [Pa], specific enthalpy h [J/kg]:

    wspWATERSTATEAREAPH(p, h)

  51. Water State Area as function of: pressure p [Pa], specific entropy s [J/(kg·K)]:

    wspWATERSTATEAREAPS(p, s)

  52. Joule-Thompson coefficient of steam at saturation line [K/Pa] as function of: temperature t [K]:

    wspJOULETHOMPSONSST(t)

  53. Joule-Thompson coefficient of water at saturation line [K/Pa] as function of: temperature t [K]:

    wspJOULETHOMPSONSWT(t)

  54. Joule-Thompson coefficient in double phase area [K/Pa] as function of: temperature t [K], degree of dryness x []:

    wspJOULETHOMPSONSTX(t, x)

  55. Degree of dryness as function of: temperature t [K], Joule-Thomspon coefficient jt [K/Pa]:

    wspXSTJOULETHOMPSON(t, jt)

  56. Set and return internal tolerance of the WaterSteamPro as function of: tolerance tolerance []:

    wspSETTOLERANCE(tolerance)

  57. Internal tolerance of the WaterSteamPro:

    wspGETTOLERANCE()

  58. Set and return a mode of management of tolerance as function of: mode mode []:

    wspSETTOLERANCEMODE(mode)

  59. Mode of management of tolerance:

    wspGETTOLERANCEMODE()

  60. Internal version of the WaterSteamPro:

    wspGETWSPVERSION()

Version 5.1

  1. Last error description:

    wspGETLASTERRORDESCRIPTION()

  2. Process related registration of the WaterSteamPro as function of: registration name name [], registration key key []:

    wspLOCALREGISTRATION(name, key)

Version 5.0

  1. Surface tension [N/m] as function of: temperature t [K]:

    wspSURFTENT(t)

  2. Specific volume [m3/kg] as function of: pressure p [Pa], temperature t [K]:

    wspVPT(p, t)

  3. Specific internal energy [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspUPT(p, t)

  4. Specific entropy [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspSPT(p, t)

  5. Specific enthalpy [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspHPT(p, t)

  6. Specific heat capacity at constant pressure (Cp) [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCPPT(p, t)

  7. Specific heat capacity at constant volume (Cv) [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCVPT(p, t)

  8. Sound velocity [m/sec] as function of: pressure p [Pa], temperature t [K]:

    wspWPT(p, t)

  9. Thermal conduction [W/(m·K)] as function of: pressure p [Pa], temperature t [K]:

    wspTHERMCONDPT(p, t)

  10. Dynamic viscosity [Pa·sec] as function of: pressure p [Pa], temperature t [K]:

    wspDYNVISPT(p, t)

  11. Prandtl number as function of: pressure p [Pa], temperature t [K]:

    wspPRANDTLEPT(p, t)

  12. Kinematic viscosity [m2/sec] as function of: pressure p [Pa], temperature t [K]:

    wspKINVISPT(p, t)

  13. Isoentropic exponent as function of: pressure p [Pa], temperature t [K]:

    wspKPT(p, t)

  14. Specific volume [m3/kg] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspVPTX(p, t, x)

  15. Specific internal energy [J/kg] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspUPTX(p, t, x)

  16. Specific entropy [J/(kg·K)] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspSPTX(p, t, x)

  17. Specific enthalpy [J/kg] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspHPTX(p, t, x)

  18. Specific heat capacity at constant pressure (Cp) [J/(kg·K)] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspCPPTX(p, t, x)

  19. Specific heat capacity at constant volume (Cv) [J/(kg·K)] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspCVPTX(p, t, x)

  20. Sound velocity [m/sec] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspWPTX(p, t, x)

  21. Thermal conduction [W/(m·K)] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspTHERMCONDPTX(p, t, x)

  22. Dynamic viscosity [Pa·sec] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspDYNVISPTX(p, t, x)

  23. Prandtl number as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspPRANDTLEPTX(p, t, x)

  24. Kinematic viscosity [m2/sec] as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspKINVISPTX(p, t, x)

  25. Isoentropic exponent as function of: pressure p [Pa], temperature t [K], degree of dryness x []:

    wspKPTX(p, t, x)

  26. Pressure at line between areas 2 and 3 [Pa] as function of: temperature t [K]:

    wspP23T(t)

  27. Temperature at line between areas 2 and 3 [K] as function of: pressure p [Pa]:

    wspT23P(p)

  28. Water state area as function of: pressure p [Pa], temperature t [K]:

    wspWATERSTATEAREA(p, t)

  29. Water state area (version 2) as function of: pressure p [Pa], temperature t [K]:

    wspWATERSTATEAREA2(p, t)

  30. Thermal conduction [W/(m·K)] as function of: density r [kg/m3], temperature t [K]:

    wspTHERMCONDRT(r, t)

  31. Dynamic viscosity [Pa·sec] as function of: density r [kg/m3], temperature t [K]:

    wspDYNVISRT(r, t)

  32. Specific volume in area 1 [m3/kg] as function of: pressure p [Pa], temperature t [K]:

    wspV1PT(p, t)

  33. Specific internal energy in area 1 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspU1PT(p, t)

  34. Specific entropy in area 1 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspS1PT(p, t)

  35. Specific enthalpy in area 1 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspH1PT(p, t)

  36. Specific heat capacity at constant pressure (Cp) in area 1 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCP1PT(p, t)

  37. Specific heat capacity at constant volume (Cv) in area 1 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCV1PT(p, t)

  38. Sound velocity in area 1 [m/sec] as function of: pressure p [Pa], temperature t [K]:

    wspW1PT(p, t)

  39. Specific volume in area 2 [m3/kg] as function of: pressure p [Pa], temperature t [K]:

    wspV2PT(p, t)

  40. Specific internal energy in area 2 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspU2PT(p, t)

  41. Specific entropy in area 2 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspS2PT(p, t)

  42. Specific enthalpy in area 2 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspH2PT(p, t)

  43. Specific heat capacity at constant pressure (Cp) in area 2 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCP2PT(p, t)

  44. Specific heat capacity at constant volume (Cv) in area 2 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCV2PT(p, t)

  45. Sound velocity in area 2 [m/sec] as function of: pressure p [Pa], temperature t [K]:

    wspW2PT(p, t)

  46. Pressure in area 3 [Pa] as function of: density r [kg/m3], temperature t [K]:

    wspP3RT(r, t)

  47. Density in area 3 [kg/m3] as function of: pressure p [Pa], temperature t [K], initial density r0 [kg/m3]:

    wspR3PTR0(p, t, r0)

  48. Density in area 3 [kg/m3] as function of: pressure p [Pa], temperature t [K]:

    wspR3PT(p, t)

  49. Specific internal energy in area 3 [J/kg] as function of: density r [kg/m3], temperature t [K]:

    wspU3RT(r, t)

  50. Specific entropy in area 3 [J/(kg·K)] as function of: density r [kg/m3], temperature t [K]:

    wspS3RT(r, t)

  51. Specific enthalpy in area 3 [J/kg] as function of: density r [kg/m3], temperature t [K]:

    wspH3RT(r, t)

  52. Specific heat capacity at constant pressure (Cp) in area 3 [J/(kg·K)] as function of: density r [kg/m3], temperature t [K]:

    wspCP3RT(r, t)

  53. Specific heat capacity at constant volume (Cv) in area 3 [J/(kg·K)] as function of: density r [kg/m3], temperature t [K]:

    wspCV3RT(r, t)

  54. Sound velocity in area 3 [m/sec] as function of: density r [kg/m3], temperature t [K]:

    wspW3RT(r, t)

  55. Specific volume in area 3 [m3/kg] as function of: pressure p [Pa], temperature t [K]:

    wspV3PT(p, t)

  56. Specific internal energy in area 3 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspU3PT(p, t)

  57. Specific entropy in area 3 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspS3PT(p, t)

  58. Specific enthalpy in area 3 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspH3PT(p, t)

  59. Specific heat capacity at constant pressure (Cp) in area 3 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCP3PT(p, t)

  60. Specific heat capacity at constant volume (Cv) in area 3 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCV3PT(p, t)

  61. Sound velocity in area 3 [m/sec] as function of: pressure p [Pa], temperature t [K]:

    wspW3PT(p, t)

  62. Specific volume in area 5 [m3/kg] as function of: pressure p [Pa], temperature t [K]:

    wspV5PT(p, t)

  63. Specific internal energy in area 5 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspU5PT(p, t)

  64. Specific entropy in area 5 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspS5PT(p, t)

  65. Specific enthalpy in area 5 [J/kg] as function of: pressure p [Pa], temperature t [K]:

    wspH5PT(p, t)

  66. Specific heat capacity at constant pressure (Cp) in area 5 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCP5PT(p, t)

  67. Specific heat capacity at constant volume (Cv) in area 5 [J/(kg·K)] as function of: pressure p [Pa], temperature t [K]:

    wspCV5PT(p, t)

  68. Sound velocity in area 5 [m/sec] as function of: pressure p [Pa], temperature t [K]:

    wspW5PT(p, t)

  69. Pressure at saturation line [Pa] as function of: temperature t [K]:

    wspPST(t)

  70. Temperature at saturation line [K] as function of: pressure p [Pa]:

    wspTSP(p)

  71. Specific volume of steam at saturation line [m3/kg] as function of: temperature t [K]:

    wspVSST(t)

  72. Specific volume of water at saturation line [m3/kg] as function of: temperature t [K]:

    wspVSWT(t)

  73. Specific internal energy of steam at saturation line [J/kg] as function of: temperature t [K]:

    wspUSST(t)

  74. Specific internal energy of water at saturation line [J/kg] as function of: temperature t [K]:

    wspUSWT(t)

  75. Specific entropy of steam at saturation line [J/(kg·K)] as function of: temperature t [K]:

    wspSSST(t)

  76. Specific entropy of water at saturation line [J/(kg·K)] as function of: temperature t [K]:

    wspSSWT(t)

  77. Specific enthalpy of steam at saturation line [J/kg] as function of: temperature t [K]:

    wspHSST(t)

  78. Specific enthalpy of water at saturation line [J/kg] as function of: temperature t [K]:

    wspHSWT(t)

  79. Specific heat capacity at constant pressure (Cp) of steam at saturation line [J/(kg·K)] as function of: temperature t [K]:

    wspCPSST(t)

  80. Specific heat capacity at constant pressure (Cp) of water at saturation line [J/(kg·K)] as function of: temperature t [K]:

    wspCPSWT(t)

  81. Specific heat capacity at constant volume (Cv) of steam at saturation line from the one-phase region= [J/(kg·K)] as function of: temperature t [K]:

    wspCVSST(t)

  82. Specific heat capacity at constant volume (Cv) of water at saturation line from the one-phase region= [J/(kg·K)] as function of: temperature t [K]:

    wspCVSWT(t)

  83. Sound velocity in steam at saturation line [m/sec] as function of: temperature t [K]:

    wspWSST(t)

  84. Sound velocity in water at saturation line [m/sec] as function of: temperature t [K]:

    wspWSWT(t)

  85. Thermal conduction of steam at saturation line [W/(m·K)] as function of: temperature t [K]:

    wspTHERMCONDSST(t)

  86. Thermal conduction of water at saturation line [W/(m·K)] as function of: temperature t [K]:

    wspTHERMCONDSWT(t)

  87. Dynamic viscosity of steam at saturation line [Pa·sec] as function of: temperature t [K]:

    wspDYNVISSST(t)

  88. Dynamic viscosity of water at saturation line [Pa·sec] as function of: temperature t [K]:

    wspDYNVISSWT(t)

  89. Prandtl number of steam at saturation line as function of: temperature t [K]:

    wspPRANDTLESST(t)

  90. Prandtl number of water at saturation line as function of: temperature t [K]:

    wspPRANDTLESWT(t)

  91. Kinematic viscosity of steam at saturation line [m2/sec] as function of: temperature t [K]:

    wspKINVISSST(t)

  92. Kinematic viscosity of water at saturation line [m2/sec] as function of: temperature t [K]:

    wspKINVISSWT(t)

  93. Isoentropic exponent of steam at saturation line as function of: temperature t [K]:

    wspKSST(t)

  94. Isoentropic exponent of water at saturation line as function of: temperature t [K]:

    wspKSWT(t)

  95. Specific evaporation heat [J/kg] as function of: temperature t [K]:

    wspRST(t)

  96. Specific volume in double phase area [m3/kg] as function of: temperature t [K], degree of dryness x []:

    wspVSTX(t, x)

  97. Specific internal energy in double phase area [J/kg] as function of: temperature t [K], degree of dryness x []:

    wspUSTX(t, x)

  98. Specific entropy in double phase area [J/(kg·K)] as function of: temperature t [K], degree of dryness x []:

    wspSSTX(t, x)

  99. Specific enthalpy in double phase area [J/kg] as function of: temperature t [K], degree of dryness x []:

    wspHSTX(t, x)

  100. Specific heat capacity at constant pressure (Cp) in double phase area [J/(kg·K)] as function of: temperature t [K], degree of dryness x []:

    wspCPSTX(t, x)

  101. Specific heat capacity at constant volume (Cv) in double phase area [J/(kg·K)] as function of: temperature t [K], degree of dryness x []:

    wspCVSTX(t, x)

  102. Sound velocity in double phase area [m/sec] as function of: temperature t [K], degree of dryness x []:

    wspWSTX(t, x)

  103. Thermal conduction in double phase area [W/(m·K)] as function of: temperature t [K], degree of dryness x []:

    wspTHERMCONDSTX(t, x)

  104. Dynamic viscosity in double phase area [Pa·sec] as function of: temperature t [K], degree of dryness x []:

    wspDYNVISSTX(t, x)

  105. Prandtl number in double phase area as function of: temperature t [K], degree of dryness x []:

    wspPRANDTLESTX(t, x)

  106. Kinematic viscosity in double phase area [m2/sec] as function of: temperature t [K], degree of dryness x []:

    wspKINVISSTX(t, x)

  107. Isoentropic exponent in double phase area as function of: temperature t [K], degree of dryness x []:

    wspKSTX(t, x)

  108. Degree of dryness as function of: temperature t [K], specific volume v [m3/kg]:

    wspXSTV(t, v)

  109. Degree of dryness as function of: temperature t [K], specific internal energy u [J/kg]:

    wspXSTU(t, u)

  110. Degree of dryness as function of: temperature t [K], specific entropy s [J/(kg·K)]:

    wspXSTS(t, s)

  111. Degree of dryness as function of: temperature t [K], specific enthalpy h [J/kg]:

    wspXSTH(t, h)

  112. Degree of dryness as function of: temperature t [K], specific heat capacity at constant pressure (Cp) cp [J/(kg·K)]:

    wspXSTCP(t, cp)

  113. Degree of dryness as function of: temperature t [K], specific heat capacity at constant volume (Cv) cv [J/(kg·K)]:

    wspXSTCV(t, cv)

  114. Degree of dryness as function of: temperature t [K], sound velocity w [m/sec]:

    wspXSTW(t, w)

  115. Degree of dryness as function of: temperature t [K], thermal conduction tc [W/(m·K)]:

    wspXSTTHERMCOND(t, tc)

  116. Degree of dryness as function of: temperature t [K], dynamic viscosity dv [Pa·sec]:

    wspXSTDYNVIS(t, dv)

  117. Degree of dryness as function of: temperature t [K], kinematic viscosity kv [m2/sec]:

    wspXSTKINVIS(t, kv)

  118. Degree of dryness as function of: temperature t [K], Prandtl number pr []:

    wspXSTPRANDTLE(t, pr)

  119. Degree of dryness as function of: temperature t [K], Isoentropic exponent k []:

    wspXSTK(t, k)

  120. Set and return a mode of checking the range of functions arguments as function of: mode mode []:

    wspSETCHECKRANGEMODE(mode)

  121. Mode of checking the range of functions arguments:

    wspGETCHECKRANGEMODE()

  122. Set and return a last error code as function of: error code ErrCode []:

    wspSETLASTERROR(ErrCode)

  123. Last error code:

    wspGETLASTERROR()

  124. Set and return maximum difference between saturation temperature and input temperature for function wspWATERSTATEAREA [K] as function of: delta delta [K]:

    wspSETDELTATS(delta)

  125. Maximum difference between saturation temperature and input temperature for function wspWATERSTATEAREA [K]:

    wspGETDELTATS()

  126. Set and return maximum iteration's count for Newton method as function of: maximum iteration maxiteration []:

    wspSETMAXITERATION(maxiteration)

  127. Maximum iteration's count for Newton method:

    wspGETMAXITERATION()

  128. Set and return maximum difference between pressure values at estimation of the area 3 parameters [Pa] as function of: delta pressure delta [Pa]:

    wspSETDELTAPRESSURE(delta)

  129. Maximum difference between pressure values at estimation of the area 3 parameters [Pa]:

    wspGETDELTAPRESSURE()

  130. Set and return initial value for water in area 3 [kg/m3] as function of: density r [kg/m3]:

    wspSETINITWATERDENSITY(r)

  131. Initial value for water in area 3 [kg/m3]:

    wspGETINITWATERDENSITY()

  132. Set and return the initial value for steam in area 3 [kg/m3] as function of: density r [kg/m3]:

    wspSETINITSTEAMDENSITY(r)

  133. Initial value for steam in area 3 [kg/m3]:

    wspGETINITSTEAMDENSITY()