WaterSteamPro Custom Units functions history list:

• Version 6.0
• Version 5.6
• Version 5.5
• Version 5.4
• Version 5.3
• Version 5.2
• Version 5.1
• Version 5.0

Version 6.0

1. Pressure [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuPHS(h, s)

2. Temperature [unit type: temperature, unit id = 2, dimension in SI: K] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuTHS(h, s)

3. Properties calculation result (p, t) as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuPTHS(h, s, *p, *t)

4. Specific volume [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuVHS(h, s)

5. Specific internal energy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuUHS(h, s)

6. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuCPHS(h, s)

7. Specific isochoric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuCVHS(h, s)

8. Sound velocity [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuWHS(h, s)

9. Joule-Tompson coefficient [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuJOULETHOMPSONHS(h, s)

10. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuTHERMCONDHS(h, s)

11. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuDYNVISHS(h, s)

12. Prandtl number [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuPRANDTLEHS(h, s)

13. Kinematic viscosity [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuKINVISHS(h, s)

14. Isoentropic exponent [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuKHS(h, s)

15. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuXHS(h, s)

16. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuXPH(p, h)

17. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuXPS(p, s)

18. Pressure in area 1 [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuP1HS(h, s)

19. Temperature in area 1 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT1HS(h, s)

20. Properties calculation result in area 1 (p, t) as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuPT1RH(r, h, *p, *t)

21. Pressure in area 2 [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuP2HS(h, s)

22. Temperature in area 2 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT2HS(h, s)

23. Properties calculation result in area 2 (p, t) as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuPT2RH(r, h, *p, *t)

24. Pressure in area 3 [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuP3HS(h, s)

25. Temperature in area 3 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT3HS(h, s)

26. Specific volume in area 3 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuV3HS(h, s)

27. Specific volume in area 3 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuV3PH(p, h)

28. Specific volume in area 3 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuV3PS(p, s)

29. Temperature in area 3 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT3RH(r, h)

30. Properties calculation result in area 5 (p, t) as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuPT5RH(r, h, *p, *t)

31. Area of phase state as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuPHASESTATEPT(p, t)

32. Water state area as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuWATERSTATEAREAHS(h, s)

33. Temperature at boundary line between areas 2 and 3 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuTB23HS(h, s)

34. Pressure at boundary line between areas 2 and 3 [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuPB23HS(h, s)

35. Specific enthalpy at boundary line between areas 1 and 3 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuHB13S(s)

36. Pressure in area 5 [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuP5HS(h, s)

37. Temperature in area 5 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT5HS(h, s)

38. Properties calculation result in area 1 (p, t) as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuPT1HS(h, s, *p, *t)

39. Properties calculation result in area 2 (p, t) as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuPT2HS(h, s, *p, *t)

40. Properties calculation result in area 3 (r, t) as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuRT3HS(h, s, *r, *t)

41. Properties calculation result in area 3 (p, t) as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuPT3HS(h, s, *p, *t)

42. Properties calculation result in area 5 (p, t) as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuPT5HS(h, s, *p, *t)

43. Rough value of density of steam at saturation line [unit type: density, unit id = 16, dimension in SI: kg/m3] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuROUGHRSST(t)

44. Rough value of density of water at saturation line [unit type: density, unit id = 16, dimension in SI: kg/m3] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuROUGHRSWT(t)

45. Specific enthalpy of steam at saturation line [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuROUGHHSSS(s)

46. Specific enthalpy of water at saturation line [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuROUGHHSWS(s)

47. Temperature at saturation line [unit type: temperature, unit id = 2, dimension in SI: K] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuTSHS(h, s)

48. Properties calculation result in double-phase area (t, x) as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuTXSHS(h, s, *t, *x)

49. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: identificator of gas/mixture id , temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcugCPIDT(id, t)

50. Specific enthalpy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: identificator of gas/mixture id , temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcugHIDT(id, t)

51. Specific entropy [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: identificator of gas/mixture id , temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcugS0IDT(id, t)

52. Molar mass [unit type: molar mass, unit id = 17, dimension in SI: kg/mole] as function of: identificator of gas/mixture id :

    wcugMMID(id)

53. Specific entropy [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: identificator of gas/mixture id , pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcugSIDPT(id, p, t)

54. New mixture identificator (id):

    wcugNEWMIX()

55. Addition of gas to mixture as function of: mixture identificator (id) mix_id , existing gas identificator (id) gas_id , gas mass mass [unit type: mass, unit id = 18, dimension in SI: kg]:

    wcugADDGASM2MIX(mix_id, gas_id, mass)

56. Addition of gas to mixture as function of: mixture identificator (id) mix_id , existing gas identificator (id) gas_id , moles of gas moles :

    wcugADDGASMO2MIX(mix_id, gas_id, moles)

57. Identificator (id) of new gas from mixture as function of: mixture identificator (id) mix_id :

    wcugNEWGASFROMMIX(mix_id)

58. Removal of existing gas as function of: gas identificator (id) id :

    wcugDELETEGAS(id)

59. Removal of existing mixture as function of: mixture identificator (id) id :

    wcugDELETEMIX(id)

60. Removal of all user-added gases:

    wcugDELETEALLGASES()

61. Removal of all mixtures:

    wcugDELETEALLMIX()

62. Gases count:

    wcugGETGASESCOUNT()

63. Mixtures count:

    wcugGETMIXCOUNT()

64. Set custom unit type parameters as function of: identificator of unit type unit_id , factor of proportionality a , addition b :

    wcuSETCU(unit_id, a, b)

65. Return custom unit type parameters (a, b) as function of: identificator of unit type unit_id :

    wcuGETCU(unit_id, *a, *b)

66. Dimension in custom units system as function of: identificator of unit type unit_id , unit dimension in SI unit_value :

    wcuSI2CU(unit_id, unit_value)

67. Dimension in SU as function of: identificator of unit type unit_id , unit dimension in custom units system unit_value :

    wcuCU2SI(unit_id, unit_value)

68. Factor of proportionality as function of: identificator of unit type unit_id :

    wcuGETCUA(unit_id)

69. Addition as function of: identificator of unit type unit_id :

    wcuGETCUB(unit_id)

70. Last error description:

    wcuGETLASTERRORDESCRIPTIONW()

71. Process related registration of the WaterSteamPro Custom Units as function of: registration name name , registration data data :

    wcuLOCALREGISTRATIONEXA(name, data)

72. Process related registration of the WaterSteamPro Custom Units as function of: registration name name , registration data data :

    wcuLOCALREGISTRATIONEXW(name, data)

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 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVUSHCVWDERPTPT(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 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVUSHCVWDERPT1PT(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 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVUSHCVWDERPT2PT(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 [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVUSHCVWDERPT3RT(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 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVUSHCVWDERPT3PT(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 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVUSHCVWDERPT5PT(p, t, *v, *u, *s, *h, *Cv, *w, *DVDPt, *DUDPt, *DSDPt, *DHDPt, *DVDTp, *DUDTp, *DSDTp, *DHDTp)

7. Derivative of saturation pressure on saturation temperature [unit type: DPDT, unit id = 19, dimension in SI: Pa/K] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuDPDTST(t)

8. Specific isochoric heat capacity of steam at saturation line from the double-phase region [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuCVDPSST(t)

9. Specific isochoric heat capacity of water at saturation line from the double-phase region [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuCVDPSWT(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 [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuVUSHCVWDERPTSWT(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 [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuVUSHCVWDERPTSST(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 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVMSPT(p, t)

2. Specific internal energy of meta-stable supercooled steam [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuUMSPT(p, t)

3. Specific entropy of meta-stable supercooled steam [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuSMSPT(p, t)

4. Specific enthalpy of meta-stable supercooled steam [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuHMSPT(p, t)

5. Specific isobaric heat capacity of meta-stable supercooled steam [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuCPMSPT(p, t)

6. Specific isochoric heat capacity of meta-stable supercooled steam [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuCVMSPT(p, t)

7. Sound velocity of meta-stable supercooled steam [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuWMSPT(p, t)

8. Thermal conductivity coefficient of meta-stable supercooled steam [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuTHERMCONDMSPT(p, t)

9. Dynamic viscosity of meta-stable supercooled steam [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuDYNVISMSPT(p, t)

10. Prandtl number of meta-stable supercooled steam [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuPRANDTLEMSPT(p, t)

11. Kinematic viscosity of meta-stable supercooled steam [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKINVISMSPT(p, t)

12. Isoentropic exponent of meta-stable supercooled steam [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKMSPT(p, t)

13. Joule-Tompson coefficient of meta-stable supercooled steam [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSONMSPT(p, t)

Version 5.4

1. Temperature [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

2. Specific volume [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

3. Specific internal energy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

4. Specific enthalpy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

5. Specific entropy [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

6. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

7. Specific isochoric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

8. Sound velocity [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

9. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

10. Kinematic viscosity [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

11. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

12. Prandtl number [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

13. Isoentropic exponent [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

14. Joule-Tompson coefficient [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

15. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction in initial point x0 [unit type: vapor fraction, unit id = 3, dimension in SI: ], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

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

16. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

    wcuXEXPANSIONPTPEFF(p0, t0, p1, eff)

Version 5.3

1. Temperature [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuTEXPANSIONPTPEFF(p0, t0, p1, eff)

2. Specific volume [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuVEXPANSIONPTPEFF(p0, t0, p1, eff)

3. Specific internal energy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuUEXPANSIONPTPEFF(p0, t0, p1, eff)

4. Specific enthalpy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuHEXPANSIONPTPEFF(p0, t0, p1, eff)

5. Specific entropy [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuSEXPANSIONPTPEFF(p0, t0, p1, eff)

6. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuCPEXPANSIONPTPEFF(p0, t0, p1, eff)

7. Specific isochoric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuCVEXPANSIONPTPEFF(p0, t0, p1, eff)

8. Sound velocity [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuWEXPANSIONPTPEFF(p0, t0, p1, eff)

9. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

   wcuTHERMCONDEXPANSIONPTPEFF(p0, t0, p1, eff)

10. Kinematic viscosity [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

    wcuKINVISEXPANSIONPTPEFF(p0, t0, p1, eff)

11. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

    wcuDYNVISEXPANSIONPTPEFF(p0, t0, p1, eff)

12. Prandtl number [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

    wcuPRANDTLEEXPANSIONPTPEFF(p0, t0, p1, eff)

13. Isoentropic exponent [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

    wcuKEXPANSIONPTPEFF(p0, t0, p1, eff)

14. Joule-Tompson coefficient [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure in initial point p0 [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature in initial point t0 [unit type: temperature, unit id = 2, dimension in SI: K], pressure in final point p1 [unit type: pressure, unit id = 1, dimension in SI: Pa], internal efficiency eff [unit type: efficiency, unit id = 15, dimension in SI: ]:

    wcuJOULETHOMPSONEXPANSIONPTPEFF(p0, t0, p1, eff)

Version 5.2

1. Joule-Tompson coefficient [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuJOULETHOMPSONPT(p, t)

2. Joule-Tompson coefficient [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

   wcuJOULETHOMPSONPTX(p, t, x)

3. Temperature [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

   wcuTPH(p, h)

4. Temperature [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

   wcuTPS(p, s)

5. Specific internal energy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

   wcuUPH(p, h)

6. Specific volume [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

   wcuVPH(p, h)

7. Specific entropy [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

   wcuSPH(p, h)

8. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

   wcuCPPH(p, h)

9. Specific isochoric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

   wcuCVPH(p, h)

10. Sound velocity [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuWPH(p, h)

11. Joule-Tompson coefficient [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuJOULETHOMPSONPH(p, h)

12. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuDYNVISPH(p, h)

13. Kinematic viscosity [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuKINVISPH(p, h)

14. Prandtl number [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuPRANDTLEPH(p, h)

15. Isoentropic exponent [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuKPH(p, h)

16. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuTHERMCONDPH(p, h)

17. Specific internal energy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuUPS(p, s)

18. Specific volume [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuVPS(p, s)

19. Specific enthalpy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuHPS(p, s)

20. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuCPPS(p, s)

21. Specific isochoric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuCVPS(p, s)

22. Sound velocity [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuWPS(p, s)

23. Joule-Tompson coefficient [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuJOULETHOMPSONPS(p, s)

24. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuDYNVISPS(p, s)

25. Kinematic viscosity [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuKINVISPS(p, s)

26. Prandtl number [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuPRANDTLEPS(p, s)

27. Isoentropic exponent [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuKPS(p, s)

28. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuTHERMCONDPS(p, s)

29. Joule-Tompson coefficient in area 1 [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSON1PT(p, t)

30. Joule-Tompson coefficient in area 2 [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSON2PT(p, t)

31. Joule-Tompson coefficient in area 3 [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSON3RT(r, t)

32. Joule-Tompson coefficient in area 3 [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSON3PT(p, t)

33. Joule-Tompson coefficient in area 5 [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSON5PT(p, t)

34. Temperature in area 1 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT1PH(p, h)

35. Temperature in area 1 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT1PS(p, s)

36. Temperature in area 2a [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT2APH(p, h)

37. Temperature in area 2a [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT2APS(p, s)

38. Temperature in area 2b [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT2BPH(p, h)

39. Temperature in area 2b [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT2BPS(p, s)

40. Temperature in area 2c [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT2CPH(p, h)

41. Temperature in area 2c [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT2CPS(p, s)

42. Temperature in area 2 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT2PH(p, h)

43. Temperature in area 2 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT2PS(p, s)

44. Temperature in area 3 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT3PH(p, h)

45. Temperature in area 3 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT3PS(p, s)

46. Temperature in area 5 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuT5PH(p, h)

47. Temperature in area 5 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuT5PS(p, s)

48. Pressure at line between areas 2b and 2c [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuP2B2CH(h)

49. Specific enthalpy at line between areas 2b and 2c [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa]:

    wcuH2B2CP(p)

50. Water state area as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

    wcuWATERSTATEAREAPH(p, h)

51. Water state area as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

    wcuWATERSTATEAREAPS(p, s)

52. Joule-Tompson coefficient of steam at saturation line [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSONSST(t)

53. Joule-Tompson coefficient of water at saturation line [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuJOULETHOMPSONSWT(t)

54. Joule-Tompson coefficient in double-phase area [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuJOULETHOMPSONSTX(t, x)

55. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], Joule-Tompson coefficient jt [unit type: joule-tompson coefficient, unit id = 8, dimension in SI: K/Pa]:

    wcuXSTJOULETHOMPSON(t, jt)

56. Set and return relative precision in the WaterSteamPro Custom Units functions [unit type: tolerance, unit id = 25, dimension in SI: ] as function of: tolerance tolerance [unit type: tolerance, unit id = 25, dimension in SI: ]:

    wcuSETTOLERANCE(tolerance)

57. Relative precision in the WaterSteamPro Custom Units functions [unit type: tolerance, unit id = 25, dimension in SI: ]:

    wcuGETTOLERANCE()

58. Set and return a mode of management of make function results more precise as function of: mode mode :

    wcuSETTOLERANCEMODE(mode)

59. Mode of management of make function results more precise:

    wcuGETTOLERANCEMODE()

60. Internal version of the WaterSteamPro Custom Units:

    wcuGETWSPVERSION()

Version 5.1

1. Last error description:

   wcuGETLASTERRORDESCRIPTION()

2. Process related registration of the WaterSteamPro Custom Units as function of: registration name name , registration key key :

   wcuLOCALREGISTRATION(name, key)

Version 5.0

1. Surface tension [unit type: surface tension, unit id = 14, dimension in SI: N/m] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuSURFTENT(t)

2. Specific volume [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuVPT(p, t)

3. Specific internal energy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuUPT(p, t)

4. Specific entropy [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuSPT(p, t)

5. Specific enthalpy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuHPT(p, t)

6. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuCPPT(p, t)

7. Specific isochoric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuCVPT(p, t)

8. Sound velocity [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuWPT(p, t)

9. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

   wcuTHERMCONDPT(p, t)

10. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuDYNVISPT(p, t)

11. Prandtl number [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuPRANDTLEPT(p, t)

12. Kinematic viscosity [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKINVISPT(p, t)

13. Isoentropic exponent [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKPT(p, t)

14. Specific volume [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuVPTX(p, t, x)

15. Specific internal energy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuUPTX(p, t, x)

16. Specific entropy [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuSPTX(p, t, x)

17. Specific enthalpy [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuHPTX(p, t, x)

18. Specific isobaric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuCPPTX(p, t, x)

19. Specific isochoric heat capacity [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuCVPTX(p, t, x)

20. Sound velocity [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuWPTX(p, t, x)

21. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuTHERMCONDPTX(p, t, x)

22. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuDYNVISPTX(p, t, x)

23. Prandtl number [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuPRANDTLEPTX(p, t, x)

24. Kinematic viscosity [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuKINVISPTX(p, t, x)

25. Isoentropic exponent [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuKPTX(p, t, x)

26. Pressure at line between areas 2 and 3 [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuP23T(t)

27. Temperature at line between areas 2 and 3 [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa]:

    wcuT23P(p)

28. Water state area as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuWATERSTATEAREA(p, t)

29. Water state area (version 2) as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuWATERSTATEAREA2(p, t)

30. Thermal conductivity coefficient [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuTHERMCONDRT(r, t)

31. Dynamic viscosity [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuDYNVISRT(r, t)

32. Specific volume in area 1 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuV1PT(p, t)

33. Specific internal energy in area 1 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuU1PT(p, t)

34. Specific entropy in area 1 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuS1PT(p, t)

35. Specific enthalpy in area 1 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuH1PT(p, t)

36. Specific isobaric heat capacity in area 1 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCP1PT(p, t)

37. Specific isochoric heat capacity in area 1 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCV1PT(p, t)

38. Sound velocity in area 1 [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuW1PT(p, t)

39. Specific volume in area 2 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuV2PT(p, t)

40. Specific internal energy in area 2 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuU2PT(p, t)

41. Specific entropy in area 2 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuS2PT(p, t)

42. Specific enthalpy in area 2 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuH2PT(p, t)

43. Specific isobaric heat capacity in area 2 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCP2PT(p, t)

44. Specific isochoric heat capacity in area 2 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCV2PT(p, t)

45. Sound velocity in area 2 [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuW2PT(p, t)

46. Pressure in area 3 [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuP3RT(r, t)

47. Density in area 3 [unit type: density, unit id = 16, dimension in SI: kg/m3] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K], initial density r0 [unit type: density, unit id = 16, dimension in SI: kg/m3]:

    wcuR3PTR0(p, t, r0)

48. Density in area 3 [unit type: density, unit id = 16, dimension in SI: kg/m3] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuR3PT(p, t)

49. Specific internal energy in area 3 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuU3RT(r, t)

50. Specific entropy in area 3 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuS3RT(r, t)

51. Specific enthalpy in area 3 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuH3RT(r, t)

52. Specific isobaric heat capacity in area 3 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCP3RT(r, t)

53. Specific isochoric heat capacity in area 3 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCV3RT(r, t)

54. Sound velocity in area 3 [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuW3RT(r, t)

55. Specific volume in area 3 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuV3PT(p, t)

56. Specific internal energy in area 3 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuU3PT(p, t)

57. Specific entropy in area 3 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuS3PT(p, t)

58. Specific enthalpy in area 3 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuH3PT(p, t)

59. Specific isobaric heat capacity in area 3 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCP3PT(p, t)

60. Specific isochoric heat capacity in area 3 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCV3PT(p, t)

61. Sound velocity in area 3 [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuW3PT(p, t)

62. Specific volume in area 5 [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuV5PT(p, t)

63. Specific internal energy in area 5 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuU5PT(p, t)

64. Specific entropy in area 5 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuS5PT(p, t)

65. Specific enthalpy in area 5 [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuH5PT(p, t)

66. Specific isobaric heat capacity in area 5 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCP5PT(p, t)

67. Specific isochoric heat capacity in area 5 [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCV5PT(p, t)

68. Sound velocity in area 5 [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa], temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuW5PT(p, t)

69. Pressure at saturation line [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuPST(t)

70. Temperature at saturation line [unit type: temperature, unit id = 2, dimension in SI: K] as function of: pressure p [unit type: pressure, unit id = 1, dimension in SI: Pa]:

    wcuTSP(p)

71. Specific volume of steam at saturation line [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuVSST(t)

72. Specific volume of water at saturation line [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuVSWT(t)

73. Specific internal energy of steam at saturation line [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuUSST(t)

74. Specific internal energy of water at saturation line [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuUSWT(t)

75. Specific entropy of steam at saturation line [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuSSST(t)

76. Specific entropy of water at saturation line [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuSSWT(t)

77. Specific enthalpy of steam at saturation line [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuHSST(t)

78. Specific enthalpy of water at saturation line [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuHSWT(t)

79. Specific isobaric heat capacity of steam at saturation line [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCPSST(t)

80. Specific isobaric heat capacity of water at saturation line [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCPSWT(t)

81. Specific isochoric heat capacity of steam at saturation line from the one-phase region [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCVSST(t)

82. Specific isochoric heat capacity of water at saturation line from the one-phase region [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuCVSWT(t)

83. Sound velocity in steam at saturation line [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuWSST(t)

84. Sound velocity in water at saturation line [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuWSWT(t)

85. Thermal conductivity coefficient of steam at saturation line [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuTHERMCONDSST(t)

86. Thermal conductivity coefficient of water at saturation line [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuTHERMCONDSWT(t)

87. Dynamic viscosity of steam at saturation line [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuDYNVISSST(t)

88. Dynamic viscosity of water at saturation line [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuDYNVISSWT(t)

89. Prandtl number of steam at saturation line [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuPRANDTLESST(t)

90. Prandtl number of water at saturation line [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuPRANDTLESWT(t)

91. Kinematic viscosity of steam at saturation line [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKINVISSST(t)

92. Kinematic viscosity of water at saturation line [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKINVISSWT(t)

93. Isoentropic exponent of steam at saturation line [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKSST(t)

94. Isoentropic exponent of water at saturation line [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuKSWT(t)

95. Specific evaporation heat [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K]:

    wcuRST(t)

96. Specific volume in double-phase area [unit type: specific volume, unit id = 4, dimension in SI: m3/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuVSTX(t, x)

97. Specific internal energy in double-phase area [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuUSTX(t, x)

98. Specific entropy in double-phase area [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuSSTX(t, x)

99. Specific enthalpy in double-phase area [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

    wcuHSTX(t, x)

100. Specific isobaric heat capacity in double-phase area [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuCPSTX(t, x)

101. Specific isochoric heat capacity in double-phase area [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuCVSTX(t, x)

102. Sound velocity in double-phase area [unit type: velocity, unit id = 7, dimension in SI: m/sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuWSTX(t, x)

103. Thermal conductivity coefficient in double-phase area [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuTHERMCONDSTX(t, x)

104. Dynamic viscosity in double-phase area [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuDYNVISSTX(t, x)

105. Prandtl number in double-phase area [unit type: prandtl number, unit id = 11, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuPRANDTLESTX(t, x)

106. Kinematic viscosity in double-phase area [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuKINVISSTX(t, x)

107. Isoentropic exponent in double-phase area [unit type: isoentropic exponent, unit id = 13, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], vapor fraction x [unit type: vapor fraction, unit id = 3, dimension in SI: ]:

     wcuKSTX(t, x)

108. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], specific volume v [unit type: specific volume, unit id = 4, dimension in SI: m3/kg]:

     wcuXSTV(t, v)

109. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], specific internal energy u [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

     wcuXSTU(t, u)

110. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], specific entropy s [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

     wcuXSTS(t, s)

111. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], specific enthalpy h [unit type: specific enthalpy, unit id = 6, dimension in SI: J/kg]:

     wcuXSTH(t, h)

112. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], Specific isobaric heat capacity Cp [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

     wcuXSTCP(t, Cp)

113. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], Specific isochoric heat capacity Cv [unit type: specific entropy, unit id = 5, dimension in SI: J/(kg·K)]:

     wcuXSTCV(t, Cv)

114. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], sound velocity w [unit type: velocity, unit id = 7, dimension in SI: m/sec]:

     wcuXSTW(t, w)

115. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], thermal conductivity coefficient tc [unit type: thermal conductivity coefficient, unit id = 9, dimension in SI: W/(m·K)]:

     wcuXSTTHERMCOND(t, tc)

116. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], dynamic viscosity dv [unit type: dynamic viscosity, unit id = 10, dimension in SI: Pa·sec]:

     wcuXSTDYNVIS(t, dv)

117. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], kinematic viscosity kv [unit type: kinematic viscosity, unit id = 12, dimension in SI: m2/sec]:

     wcuXSTKINVIS(t, kv)

118. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], Prandtl number pr [unit type: prandtl number, unit id = 11, dimension in SI: ]:

     wcuXSTPRANDTLE(t, pr)

119. Vapor fraction [unit type: vapor fraction, unit id = 3, dimension in SI: ] as function of: temperature t [unit type: temperature, unit id = 2, dimension in SI: K], Isoentropic exponent k [unit type: isoentropic exponent, unit id = 13, dimension in SI: ]:

     wcuXSTK(t, k)

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

     wcuSETCHECKRANGEMODE(mode)

121. Mode of checking the range of functions arguments:

     wcuGETCHECKRANGEMODE()

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

     wcuSETLASTERROR(ErrCode)

123. Last error code:

     wcuGETLASTERROR()

124. Set and return maximum difference between saturation temperature and input temperature for function wcuWATERSTATEAREA [unit type: temperature, unit id = 2, dimension in SI: K] as function of: delta delta [unit type: temperature, unit id = 2, dimension in SI: K]:

     wcuSETDELTATS(delta)

125. Maximum difference between saturation temperature and input temperature for function wcuWATERSTATEAREA [unit type: temperature, unit id = 2, dimension in SI: K]:

     wcuGETDELTATS()

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

     wcuSETMAXITERATION(maxiteration)

127. Maximum iteration's count for Newton method:

     wcuGETMAXITERATION()

128. Set and return maximum difference between pressure values at estimation of the area 3 parameters [unit type: pressure, unit id = 1, dimension in SI: Pa] as function of: delta pressure delta [unit type: pressure, unit id = 1, dimension in SI: Pa]:

     wcuSETDELTAPRESSURE(delta)

129. Maximum difference between pressure values at estimation of the area 3 parameters [unit type: pressure, unit id = 1, dimension in SI: Pa]:

     wcuGETDELTAPRESSURE()

130. Set and return initial value for water in area 3 [unit type: density, unit id = 16, dimension in SI: kg/m3] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3]:

     wcuSETINITWATERDENSITY(r)

131. Initial value for water in area 3 [unit type: density, unit id = 16, dimension in SI: kg/m3]:

     wcuGETINITWATERDENSITY()

132. Set and return the initial value for steam in area 3 [unit type: density, unit id = 16, dimension in SI: kg/m3] as function of: density r [unit type: density, unit id = 16, dimension in SI: kg/m3]:

     wcuSETINITSTEAMDENSITY(r)

133. Initial value for steam in area 3 [unit type: density, unit id = 16, dimension in SI: kg/m3]:

     wcuGETINITSTEAMDENSITY()