S	
V	1 	ProgCtrl	7	1
* starred lines are ignored by programs
*
*   Mol Wt  Crit Temp   Crit Press  Liquid Range        Vapor Range
*       (K) (kPa)   MinT    MaxT    MinT    MaxT    MaxP
Data	18	647	22055	273.16	64515	1	1	1
*
*   Formula A   B   C   D   E
*
*Vapor Pressure (Bubble Point)
*   1   polynomial fit      Pv = A + BT + CT^2 + DT^3 + ET^4                    KPa as a function of temp K
*   2   DIPPR formula       Pv = exp(A + B/T + ClnT + DT^E)                 Pa as a function of temp K
*   3   Yaws formula        logPv = A + B/T + ClogT + D(10^3)T + E(10^6)T^2                 mm Hg as a function of temp K
*
P1	1	1.773	0	0	0	0
*
*Vapor Pressure (Dew Point)
*   0   no formula, pure substance
*   1   polynomial fit      Pv = A + BT + CT^2 + DT^3 + ET^4                    KPa as a function of temp K
*   2   DIPPR formula       Pv = exp(A + B/T + ClnT + DT^E)                 Pa as a function of temp K
*   3   Yaws formula        logPv = A + B/T + ClogT + D(10^3)T + E(10^6)T^2                 mm Hg as a function of temp K
*
P2	0	0	0	0	0	0
*
*Liquid Density
*   0   no formula, vapor only fluid
*   1   polynomial fit      Den = A + BT + CT^2 + DT^3 + ET^4                   kg/m^3 as a function of temp K
*   2   DIPPR formula       Den = A/B^[1.0 + (1.0 - T/C)^D]                 kmol/m^3 as a function of temp K
*   3   Yaws formula        Den = AB^[-(1.0 - T/Tc)^(2/7)]                  g/cm^3 as a function of temp K
*
P3	1	820	0	0	0	0
*
*Liquid Viscosity
*   0   no formula, vapor only fluid
*   1   polynomial fit      Vsc = A + BT + CT^2 + DT^3 + ET^4                   cP as a function of temp K
*   2   DIPPR formula       Vsc = exp(A + B/T + ClnT + DT^E                 Pa-s as a function of temp K
*   3   Yaws formula        log(Vsc) = A + B/T + C(10^2)T + D(10^6)T^2                  cP as a function of temp K
*
P4	1	1.4	0	0	0	0
*
*Vapor Density
*   0   no formula, liquid only fluid
*   1   Ideal gas formula, PV = nRT
*   2   Cubic eq of state - Peng-Robinson                       A = acentric factor
*   3   Cubic eq of state - Redlich-Kwong                       B = Kij factor (mixtures only)
*   4   Cubic eq of state - Soave                       C = Kji factor (mixtures only)
*
P5	0	0	0	0	0	0
*
*Vapor Viscosity
*   0   no formula, liquid only fluid
*   1   polynomial fit      Vsc = A + BT + CT^2 + DT^3 + ET^4                   cP as a function of temp K
*   2   DIPPR formula       Vsc = (AT^B)/(1 + C/T + D/T^2)                  Pa-s as a function of temp K
*   3   Yaws formula        Vsc = A + B(10^2)T + C(10^6)T^2                 microP as a function of temp K
*
P6	0	0	0	0	0	0
*
*Vapor Heat Capacity
*   0   no formula, liquid only fluid
*   1   polynomial fit      Cp = A + BT + CT^2 + DT^3 + ET^4                    KJ/kmol-K as a function of temp K
*   2   DIPPR formula       Cp = A + B[(C/T)/sinh((C/T)]^2 + D[(E/T)/cosh(E/T)]^2                   J/kmol-K as a function of temp K
*   3   Yaws formula        Cp = A + B(10^3)T + C(10^6)T^2 + D(10^9)T^3                 cal/gmol-K as a function of temp K
*
P7	0	0	0	0	0	0
*
