S	"30% Nitric acid, 70% Water: A Molecular Knowledge Systems fluid data table."								
V	2	ProgCtrl	7	1					
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*	Mw	Tc	Pc	Liquid Range		Vapor Range			
*		(K)	(kPa)	MinT	MaxT	MinT	MaxT	MaxP	
Data	22.92689197	647.13	22055	273.15	373.15	1	1	1	
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*Vapor Pressure (Bubble Point)									
*	1	Polynomial fit		Pvp = A + BT + CT^2 + DT^3 + ET^4					KPa as a function of temp K
*	2	DIPPR formula		Pvp = exp(A + B/T + ClnT + DT^E)					Pa as a function of temp K
*	3	Yaws formula		log(Pvp) = A + B/T + ClogT + D(/10^3)T + E(/10^6)T^2					mm Hg as a function of temp K
*									
*	Formula	A	B	C	D	E			
P1	2	34.65983906	-5635.399908	-1.400630661	0	0			
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*Vapor Pressure (Dew Point)									
*	0	"No formula, pure substance"							
*	1	Polynomial fit		Pvp = A + BT + CT^2 + DT^3 + ET^4					KPa as a function of temp K
*	2	DIPPR formula		Pvp = exp(A + B/T + ClnT + DT^E)					Pa as a function of temp K
*	3	Yaws formula		log(Pvp) = A + B/T + ClogT + D(/10^3)T + E(/10^6)T^2					mm Hg as a function of temp K
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*	Formula	A	B	C	D	E			
P2	0	0	0	0	0	0			
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*Liquid Density									
*	0	"No formula, pure substance"							
*	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
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*	Formula	A	B	C	D	E			
P3	1	1420.976273	-0.823636364	0	0	0			
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*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
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*	Formula	A	B	C	D	E			
P4	2	-67.33703792	4202.399609	8.16330857	0	0			
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*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)
*									
*	Formula	A	B	C	D	E			
P5	0	0	0	0	0	0			
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*									
*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
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*	Formula	A	B	C	D	E			
P6	0	0	0	0	0	0			
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*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
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*	Formula	A	B	C	D	E			
P7	0	0	0	0	0	0			
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