S	"U of Idaho ALLPROPS, DIPPR, and Yaws"								
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	647.126	22055	273.16	645.15	283.15	820	22055	
*									
*	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	3	16.373	-2818.6	-1.6908	-5.7546	4.0073			
*									
*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 °C
*									
P3	1	-2282.2826	32.520027	-0.11694663	0.00018187322	-0.00000010625727			
*									
*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 °C
*									
P4	2	-52	3670	5.7331	-5.35E-29	10			
*									
*Vapor Density									
*	0	"no formula, liquid only fluid"							
*	1	"Ideal gas formula, PV = nRT"							
*	2	Cubic eq of state - Peng-Robinson						A = acentric factor (1.0 for Redlich-Kwong)	
*	3	Cubic eq of state - Redlich-Kwong						B = Kij factor (mixtures only)	
*	4	Cubic eq of state - Soave						C = Kji factor (mixtures only)	
*									
P5	2	0.344	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 °C
*									
P6	1	0.0066667577	-0.000019785295	0.0000001376651	-1.3659501E-10	5.0620697E-14			
*									
*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	1	48.191688	-0.11985027	0.00034996877	-0.00000041865672	1.8892619E-10
*						
