IS THE INPUT DATA ON A FILE (Y/N)?
 ENTER UNITS CHOSEN FOR TEMPERATURE 
 CHOOSE FROM 1=DEG K, 2=DEG C, 3=DEG R, 4=DEG F
 ENTER UNITS CHOSEN FOR DENSITY     
 CHOOSE FROM 1=KG/M3, 2=G/CM3, 3=MOL/L, 4=LB/FT3
 ENTER UNITS CHOSEN FOR PRESSURE    
 CHOOSE FROM 1=MPA, 2=BAR, 3=ATM, 4=PSIA, 5=KG/CM2
 ENTER UNITS CHOSEN FOR ENERGY      
 CHOOSE FROM 1=KJ/KG, 2=J/G, 3=J/MOL, 4=CALORIES/G, 5=CALORIES/MOL, 6=BTU/LB


 ENTER OPTION NO., X, AND TEMPERATURE WHERE:
       1,D,T    D = DENSITY
       2,P,T    P = PRESSURE
       3, ,T    CALCULATE SATURATED VALUES AS F(T)
       4,P, ,   CALCULATE SATURATED VALUES AS F(P)
       5, , ,   CHANGE UNITS
       6, , ,   CHANGE SOURCE OF INPUT
       0, , ,   TO QUIT AND RETURN TO DOS

 IOPT =    1  X = 0.100000000000000000D+01  T = 0.300000000000000000D+03
  
 COMPR. WATER OR SUPERHEATED STEAM  T =  300.0000 DEG K     NBS/NRC STEAM TABLES
 P =     0.12905951 MPA       H =  2497.8501240 KJ/KG     DP/DT =     0.00058641
 D =     1.00000000 KG/M3     U =  2368.7906124 KJ/KG     DV/DT =     4.93292817
 V =     1.00000000           G =   484.2718274 KJ/KG     DP/DD =     0.11887755
 CP =    3.00291314 KJ/KG K   S =     6.7119277 KJ/KG K   JT(T) =  -479.87845120
 CV =    2.13509107 KJ/KG K   VEL SND =   408.9  M/SEC    JT(H) =   159.80430630
  **CAUTION - DENSITY, TEMP. DEFINE METASTABLE STATE
 PL =    0.00353573 MPA       GL=   -5.35765101 KJ/KG   DL=  996.52353877 KG/M3 
 PV =    0.00353573 MPA       GV=   -5.35765114 KJ/KG   DV=    0.02557752 KG/M3 


 ENTER OPTION NO., X, AND TEMPERATURE WHERE:
       1,D,T    D = DENSITY
       2,P,T    P = PRESSURE
       3, ,T    CALCULATE SATURATED VALUES AS F(T)
       4,P, ,   CALCULATE SATURATED VALUES AS F(P)
       5, , ,   CHANGE UNITS
       6, , ,   CHANGE SOURCE OF INPUT
       0, , ,   TO QUIT AND RETURN TO DOS

 IOPT =    2  X = 0.781723329999999980D+01  T = 0.300000000000000000D+03
  
 COMPR. WATER OR SUPERHEATED STEAM  T =  300.0000 DEG K     NBS/NRC STEAM TABLES
 P =     7.81723330 MPA       H =   119.6611650 KJ/KG     DP/DT =     0.64408686
 D =   999.99999821 KG/M3     U =   111.8439357 KJ/KG     DV/DT =     0.00028407
 V =     0.00100000           G =     2.4696162 KJ/KG     DP/DD =     2.26733130
 CP =    4.16209518 KJ/KG K   S =     0.3906385 KJ/KG K   JT(T) =     0.91477820
 CV =    4.10720494 KJ/KG K   VEL SND =  1515.8  M/SEC    JT(H) =    -0.21978791


 ENTER OPTION NO., X, AND TEMPERATURE WHERE:
       1,D,T    D = DENSITY
       2,P,T    P = PRESSURE
       3, ,T    CALCULATE SATURATED VALUES AS F(T)
       4,P, ,   CALCULATE SATURATED VALUES AS F(P)
       5, , ,   CHANGE UNITS
       6, , ,   CHANGE SOURCE OF INPUT
       0, , ,   TO QUIT AND RETURN TO DOS

 IOPT =    3  X = 0.000000000000000000D+00  T = 0.300000000000000000D+03
  
 SATURATED LIQUID PROPERTIES        T =  300.0000 DEG K     NBS/NRC STEAM TABLES
 P =     0.00353573 MPA       H =   112.4923360 KJ/KG     DP/DT =     0.61432555
 D =   996.52353877 KG/M3     U =   112.4887880 KJ/KG     DV/DT =     0.00027768
 V =     0.00100349           G =    -5.3576510 KJ/KG     DP/DD =     2.22781538
 CP =    4.18338931 KJ/KG K   S =     0.3928333 KJ/KG K   JT(T) =     0.92018465
 CV =    4.13221357 KJ/KG K   VEL SND =  1501.8  M/SEC    JT(H) =    -0.21996152
  
 SATURATED VAPOR PROPERTIES         T =  300.0000 DEG K     NBS/NRC STEAM TABLES
 P =     0.00353573 MPA       H =  2549.6293565 KJ/KG     DP/DT =     0.00001187
 D =     0.02557752 KG/M3     U =  2411.3933552 KJ/KG     DV/DT =   131.51108527
 V =    39.09682946           G =    -5.3576511 KJ/KG     DP/DD =     0.13801488
 CP =    1.88865787 KJ/KG K   S =     8.5166234 KJ/KG K   JT(T) =  -356.49612098
 CV =    1.42018030 KJ/KG K   VEL SND =   428.4  M/SEC    JT(H) =   188.75632592


 ENTER OPTION NO., X, AND TEMPERATURE WHERE:
       1,D,T    D = DENSITY
       2,P,T    P = PRESSURE
       3, ,T    CALCULATE SATURATED VALUES AS F(T)
       4,P, ,   CALCULATE SATURATED VALUES AS F(P)
       5, , ,   CHANGE UNITS
       6, , ,   CHANGE SOURCE OF INPUT
       0, , ,   TO QUIT AND RETURN TO DOS

 IOPT =    4  X = 0.781723329999999980D+01  T = 0.000000000000000000D+00
  
 SATURATED LIQUID PROPERTIES        T =  566.5830 DEG K     NBS/NRC STEAM TABLES
 P =     7.81723192 MPA       H =  1307.7619974 KJ/KG     DP/DT =     1.06452020
 D =   725.55375824 KG/M3     U =  1296.9878379 KJ/KG     DV/DT =     0.00414373
 V =     0.00137826           G =  -500.5145116 KJ/KG     DP/DD =     0.48800429
 CP =    5.56766916 KJ/KG K   S =     3.1915476 KJ/KG K   JT(T) =    -0.96950720
 CV =    3.06842609 KJ/KG K   VEL SND =   941.0  M/SEC    JT(H) =     0.17413161
  
 SATURATED VAPOR PROPERTIES         T =  566.5830 DEG K     NBS/NRC STEAM TABLES
 P =     7.81723327 MPA       H =  2760.4640778 KJ/KG     DP/DT =     0.03154523
 D =    41.40163908 KG/M3     U =  2571.6494936 KJ/KG     DV/DT =     0.15539125
 V =     0.02415363           G =  -500.5145119 KJ/KG     DP/DD =     0.11843283
 CP =    5.54651145 KJ/KG K   S =     5.7555182 KJ/KG K   JT(T) =   -63.88840170
 CV =    2.76920494 KJ/KG K   VEL SND =   487.0  M/SEC    JT(H) =    11.51866398


 ENTER OPTION NO., X, AND TEMPERATURE WHERE:
       1,D,T    D = DENSITY
       2,P,T    P = PRESSURE
       3, ,T    CALCULATE SATURATED VALUES AS F(T)
       4,P, ,   CALCULATE SATURATED VALUES AS F(P)
       5, , ,   CHANGE UNITS
       6, , ,   CHANGE SOURCE OF INPUT
       0, , ,   TO QUIT AND RETURN TO DOS