Chemical Properties of 1-Propanol (CAS 71-23-8)

InChI

InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3

InChI Key

BDERNNFJNOPAEC-UHFFFAOYSA-N

Formula

C3H8O

SMILES

CCCO

Molecular Weight¹

60.09

CAS

71-23-8

Other Names

• 1-Hydroxypropane
• 1-Propyl alcohol
• Alcohol, propyl
• Alcool propilico
• Alcool propylique
• Ethylcarbinol
• N-PROPYL ALCOHOL
• NSC 30300
• Optal
• Osmosol extra
• PROPYL ALCOHOL
• Propan-1-ol
• Propanol
• Propanol-1
• Propanole
• Propanolen
• Propanoli
• Propylan-propyl alcohol
• Propylic alcohol
• Propylowy alkohol
• UN 1274
• n-C3H7OH
• n-Propan-1-ol
• n-Propanol
• n-Propyl alkohol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.6230		KDB
PAff	786.50	kJ/mol	NIST
Tig	644.26	K	KDB
BasG	756.10	kJ/mol	NIST
ΔcH°liquid	[-2032.59; -2017.70]	kJ/mol
ΔcH°liquid	-2021.31 ± 0.25	kJ/mol	NIST
ΔcH°liquid	-2019.40 ± 0.30	kJ/mol	NIST
ΔcH°liquid	-2021.40 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-2017.70 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-2032.59	kJ/mol	NIST
Cp,liquid	143.41	J/mol×K	THERMOD...
μ	1.70	debye	KDB
η	0.0019544	Pa×s	Densiti...
LFL	2.10	% in Air	KDB
UFL	13.50	% in Air	KDB
Tflash,cc	300.37	K	KDB
Tflash,oc	298.15	K	KDB
ΔfG°	-161.90	kJ/mol	KDB
Rg	2.7360		KDB
ΔfH°gas	[-258.80; -254.70]	kJ/mol
ΔfH°gas	-256.60	kJ/mol	KDB
ΔfH°gas	-255.10	kJ/mol	NIST
ΔfH°gas	-255.20 ± 0.30	kJ/mol	NIST
ΔfH°gas	-255.60 ± 1.30	kJ/mol	NIST
ΔfH°gas	-257.20	kJ/mol	NIST
ΔfH°gas	-257.30 ± 0.40	kJ/mol	NIST
ΔfH°gas	-254.70 ± 4.40	kJ/mol	NIST
ΔfH°gas	-258.80 ± 1.10	kJ/mol	NIST
ΔfH°liquid	[-306.30; -302.50]	kJ/mol
ΔfH°liquid	-302.54 ± 0.25	kJ/mol	NIST
ΔfH°liquid	-303.00 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-304.60 ± 0.40	kJ/mol	NIST
ΔfH°liquid	-302.50 ± 4.20	kJ/mol	NIST
ΔfH°liquid	-306.30 ± 1.00	kJ/mol	NIST
ΔfusH°	5.40	kJ/mol	Heat Ca...
ΔvapH°	38.95	kJ/mol	Joback Calculated Property
IE	[10.00; 10.52]	eV
IE	10.22 ± 0.06	eV	NIST
IE	10.22 ± 0.07	eV	NIST
IE	10.00	eV	NIST
IE	10.15 ± 0.03	eV	NIST
IE	10.16 ± 0.03	eV	NIST
IE	10.32 ± 0.02	eV	NIST
IE	10.25	eV	NIST
IE	10.22 ± 0.04	eV	NIST
IE	10.20	eV	NIST
IE	10.51	eV	NIST
IE	10.52 ± 0.03	eV	NIST
IE	10.51	eV	NIST
IE	10.49	eV	NIST
IE	10.48	eV	NIST
log10WS	[0.62; 0.62]
log10WS	0.62		Aq. Sol...
log10WS	0.62		Estimat...
logPoct/wat	0.389		Crippen Calculated Property
McVol	59.000	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[5082.00; 5397.00]	kPa
Pc	5169.00	kPa	KDB
Pc	5170.00 ± 20.00	kPa	NIST
Pc	5170.00	kPa	NIST
Pc	5168.00 ± 20.00	kPa	NIST
Pc	5168.00 ± 20.00	kPa	NIST
Pc	5170.00	kPa	NIST
Pc	5182.00 ± 10.00	kPa	NIST
Pc	5155.00	kPa	NIST
Pc	5170.00	kPa	NIST
Pc	5082.00	kPa	NIST
Pc	5218.00	kPa	NIST
Pc	5082.00	kPa	NIST
Pc	Outlier 5397.00	kPa	NIST
Inp	[507.00; 595.00]
Inp	561.20		NIST
Inp	561.40		NIST
Inp	559.30		NIST
Inp	558.20		NIST
Inp	549.70		NIST
Inp	543.70		NIST
Inp	536.90		NIST
Inp	Outlier 521.00		NIST
Inp	544.60		NIST
Inp	542.30		NIST
Inp	540.50		NIST
Inp	541.50		NIST
Inp	556.50		NIST
Inp	553.60		NIST
Inp	551.40		NIST
Inp	544.60		NIST
Inp	542.30		NIST
Inp	540.50		NIST
Inp	541.50		NIST
Inp	556.50		NIST
Inp	553.50		NIST
Inp	551.40		NIST
Inp	565.00		NIST
Inp	575.00		NIST
Inp	546.00		NIST
Inp	555.00		NIST
Inp	530.00		NIST
Inp	539.90		NIST
Inp	530.00		NIST
Inp	544.00		NIST
Inp	525.00		NIST
Inp	562.00		NIST
Inp	Outlier 520.00		NIST
Inp	547.00		NIST
Inp	523.00		NIST
Inp	574.00		NIST
Inp	561.00		NIST
Inp	555.00		NIST
Inp	Outlier 595.00		NIST
Inp	551.00		NIST
Inp	568.00		NIST
Inp	560.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	524.00		NIST
Inp	Outlier 521.00		NIST
Inp	551.00		NIST
Inp	555.00		NIST
Inp	557.00		NIST
Inp	556.00		NIST
Inp	537.00		NIST
Inp	540.20		NIST
Inp	540.20		NIST
Inp	546.00		NIST
Inp	552.00		NIST
Inp	532.00		NIST
Inp	552.00		NIST
Inp	552.00		NIST
Inp	536.00		NIST
Inp	533.00		NIST
Inp	530.00		NIST
Inp	537.00		NIST
Inp	544.00		NIST
Inp	535.00		NIST
Inp	Outlier 507.00		NIST
Inp	557.00		NIST
Inp	561.00		NIST
Inp	549.00		NIST
Inp	553.00		NIST
Inp	536.00		NIST
Inp	559.00		NIST
Inp	559.00		NIST
Inp	559.00		NIST
Inp	548.00		NIST
Inp	557.90		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	554.00		NIST
Inp	553.00		NIST
Inp	560.00		NIST
Inp	539.00		NIST
Inp	538.64		NIST
Inp	Outlier 521.00		NIST
Inp	535.00		NIST
Inp	548.00		NIST
Inp	561.00		NIST
Inp	555.00		NIST
Inp	568.00		NIST
Inp	547.00		NIST
Inp	544.00		NIST
Inp	548.00		NIST
Inp	544.00		NIST
Inp	557.00		NIST
Inp	558.00		NIST
Inp	551.00		NIST
Inp	544.00		NIST
Inp	548.00		NIST
Inp	548.00		NIST
Inp	535.00		NIST
Inp	570.00		NIST
Inp	560.00		NIST
Inp	539.00		NIST
Inp	560.00		NIST
Inp	562.00		NIST
Inp	543.00		NIST
Inp	546.00		NIST
Inp	546.00		NIST
Inp	539.00		NIST
Inp	571.00		NIST
Inp	534.00		NIST
Inp	555.00		NIST
Inp	535.00		NIST
Inp	Outlier 581.00		NIST
Inp	571.00		NIST
Inp	572.00		NIST
Inp	561.20		NIST
Inp	543.70		NIST
Inp	540.50		NIST
Inp	544.60		NIST
Inp	553.50		NIST
Inp	555.00		NIST
Inp	525.00		NIST
Inp	561.00		NIST
Inp	557.00		NIST
Inp	559.00		NIST
Inp	568.00		NIST
Inp	560.00		NIST
Inp	548.00		NIST
I	[988.00; 1086.00]
I	1046.00		NIST
I	1037.00		NIST
I	1031.00		NIST
I	1024.00		NIST
I	1037.60		NIST
I	1046.90		NIST
I	1051.70		NIST
I	1054.90		NIST
I	Outlier 1072.00		NIST
I	Outlier 988.00		NIST
I	1000.00		NIST
I	Outlier 997.00		NIST
I	1040.00		NIST
I	1035.00		NIST
I	Outlier 993.00		NIST
I	1031.00		NIST
I	1030.00		NIST
I	1046.00		NIST
I	1036.00		NIST
I	1026.00		NIST
I	1056.00		NIST
I	1021.00		NIST
I	1014.00		NIST
I	Outlier 993.00		NIST
I	1037.00		NIST
I	1030.00		NIST
I	1043.00		NIST
I	1005.00		NIST
I	1002.00		NIST
I	1025.00		NIST
I	1037.00		NIST
I	1060.00		NIST
I	1061.00		NIST
I	1030.00		NIST
I	1049.00		NIST
I	1049.00		NIST
I	1025.00		NIST
I	1015.00		NIST
I	1038.00		NIST
I	1026.00		NIST
I	1045.00		NIST
I	1041.00		NIST
I	1052.00		NIST
I	1040.00		NIST
I	1045.00		NIST
I	Outlier 1073.00		NIST
I	1041.00		NIST
I	1038.00		NIST
I	1038.00		NIST
I	1064.00		NIST
I	1049.00		NIST
I	1025.00		NIST
I	1025.00		NIST
I	1031.00		NIST
I	1052.00		NIST
I	1052.00		NIST
I	1051.00		NIST
I	1052.00		NIST
I	1052.00		NIST
I	1037.00		NIST
I	1029.00		NIST
I	1041.00		NIST
I	1032.00		NIST
I	1034.00		NIST
I	1031.00		NIST
I	1033.00		NIST
I	1028.00		NIST
I	1023.00		NIST
I	1040.00		NIST
I	1037.00		NIST
I	1045.00		NIST
I	1034.00		NIST
I	1025.00		NIST
I	1035.00		NIST
I	1002.00		NIST
I	1030.00		NIST
I	1030.00		NIST
I	1043.00		NIST
I	1037.00		NIST
I	1029.00		NIST
I	1025.00		NIST
I	1040.00		NIST
I	1038.00		NIST
I	1045.00		NIST
I	1006.00		NIST
I	1038.00		NIST
I	1032.00		NIST
I	1002.00		NIST
I	1069.00		NIST
I	1046.00		NIST
I	1049.00		NIST
I	1002.00		NIST
I	1042.00		NIST
I	1022.00		NIST
I	1002.00		NIST
I	1030.00		NIST
I	Outlier 990.00		NIST
I	Outlier 996.00		NIST
I	Outlier 990.00		NIST
I	Outlier 996.00		NIST
I	1042.00		NIST
I	1040.00		NIST
I	1036.00		NIST
I	1038.00		NIST
I	1045.00		NIST
I	Outlier 992.00		NIST
I	1030.00		NIST
I	1036.00		NIST
I	Outlier 1086.00		NIST
I	1036.00		NIST
I	1036.00		NIST
I	1051.00		NIST
I	1052.00		NIST
I	1046.00		NIST
I	1036.00		NIST
I	1036.00		NIST
I	1036.00		NIST
I	1032.00		NIST
I	1035.00		NIST
I	1044.00		NIST
I	1036.00		NIST
I	1038.00		NIST
I	1042.00		NIST
I	1036.00		NIST
I	1042.00		NIST
I	1042.00		NIST
I	1047.00		NIST
I	1042.00		NIST
I	1025.00		NIST
I	1027.00		NIST
I	1031.00		NIST
I	1002.00		NIST
I	Outlier 1072.00		NIST
I	1033.00		NIST
I	1033.00		NIST
I	1014.00		NIST
I	1040.00		NIST
I	1030.00		NIST
I	1051.00		NIST
I	1036.00		NIST
I	1038.00		NIST
I	1047.00		NIST
I	1002.00		NIST
I	1037.00		NIST
I	1025.00		NIST
I	1049.00		NIST
I	1026.00		NIST
I	1045.00		NIST
I	1064.00		NIST
I	1052.00		NIST
I	1031.00		NIST
I	1046.00		NIST
I	1046.90		NIST
I	1000.00		NIST
I	1056.00		NIST
S°gas	322.49	J/mol×K	NIST
S°liquid	[192.80; 214.20]	J/mol×K
S°liquid	192.80	J/mol×K	NIST
S°liquid	214.20	J/mol×K	NIST
S°solid,1 bar	112.70	J/mol×K	NIST
Tboil	[355.30; 371.25]	K
Tboil	370.30	K	KDB
Tboil	370.40	K	Excess ...
Tboil	370.44	K	Isobari...
Tboil	370.31	K	Isobari...
Tboil	370.35	K	Isobari...
Tboil	370.20	K	Heterog...
Tboil	369.75	K	Isobari...
Tboil	370.45	K	(Vapour...
Tboil	370.35	K	Isobari...
Tboil	369.90	K	Separat...
Tboil	370.35	K	Measure...
Tboil	370.33	K	Isobari...
Tboil	370.30	K	Isobari...
Tboil	370.31	K	Measure...
Tboil	370.19	K	Vapor-L...
Tboil	370.21	K	Vapor-L...
Tboil	370.24	K	Vapor-L...
Tboil	370.05	K	P, rho,...
Tboil	370.40	K	Evaluat...
Tboil	370.21	K	Vapor-L...
Tboil	370.21	K	Vapor L...
Tboil	370.30 ± 0.20	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.20 ± 0.40	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.26 ± 0.20	K	NIST
Tboil	370.28 ± 0.08	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	370.40 ± 0.20	K	NIST
Tboil	370.30 ± 0.30	K	NIST
Tboil	370.10 ± 0.25	K	NIST
Tboil	370.60	K	NIST
Tboil	370.50 ± 0.20	K	NIST
Tboil	370.30	K	NIST
Tboil	370.40 ± 0.40	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.15 ± 0.50	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.32 ± 0.06	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.29 ± 0.30	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.35 ± 0.20	K	NIST
Tboil	370.23 ± 0.12	K	NIST
Tboil	370.50 ± 0.30	K	NIST
Tboil	370.35 ± 0.30	K	NIST
Tboil	370.35	K	NIST
Tboil	370.35 ± 0.30	K	NIST
Tboil	370.25 ± 0.20	K	NIST
Tboil	370.44 ± 0.15	K	NIST
Tboil	370.30 ± 0.05	K	NIST
Tboil	370.40 ± 0.20	K	NIST
Tboil	370.23 ± 0.20	K	NIST
Tboil	370.00 ± 1.50	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	370.35 ± 0.30	K	NIST
Tboil	370.38 ± 0.10	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.34 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.70 ± 1.00	K	NIST
Tboil	366.70 ± 3.00	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.00 ± 0.50	K	NIST
Tboil	370.59 ± 0.33	K	NIST
Tboil	370.40 ± 0.20	K	NIST
Tboil	370.20 ± 0.30	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	368.70 ± 1.00	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	368.60 ± 1.00	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.34 ± 0.20	K	NIST
Tboil	367.60 ± 1.00	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	369.60 ± 0.50	K	NIST
Tboil	Outlier 355.40 ± 0.30	K	NIST
Tboil	370.10 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.40	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	371.20 ± 0.50	K	NIST
Tboil	370.70 ± 0.60	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	Outlier 355.30 ± 0.50	K	NIST
Tboil	369.60 ± 1.00	K	NIST
Tboil	369.80 ± 0.40	K	NIST
Tboil	371.00 ± 0.30	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	369.60 ± 1.00	K	NIST
Tboil	370.35 ± 0.03	K	NIST
Tboil	370.95 ± 0.10	K	NIST
Tboil	370.30 ± 0.30	K	NIST
Tboil	370.30 ± 0.05	K	NIST
Tboil	370.40 ± 0.10	K	NIST
Tboil	370.34 ± 0.07	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.70 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.70 ± 1.00	K	NIST
Tboil	370.31 ± 0.30	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.70 ± 1.00	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	371.00 ± 0.30	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.20 ± 0.50	K	NIST
Tboil	370.34 ± 0.10	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.90 ± 0.20	K	NIST
Tboil	370.13 ± 0.20	K	NIST
Tboil	370.30 ± 0.20	K	NIST
Tboil	371.25 ± 0.20	K	NIST
Tboil	370.34 ± 0.05	K	NIST
Tboil	370.33 ± 0.05	K	NIST
Tboil	370.35 ± 0.05	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.20 ± 0.50	K	NIST
Tboil	369.80 ± 0.30	K	NIST
Tboil	369.90 ± 0.50	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.37 ± 0.10	K	NIST
Tboil	369.60 ± 1.00	K	NIST
Tboil	370.30 ± 0.50	K	NIST
Tboil	370.60 ± 0.30	K	NIST
Tboil	370.41 ± 0.20	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.40 ± 0.30	K	NIST
Tboil	370.50 ± 0.50	K	NIST
Tboil	370.00 ± 1.00	K	NIST
Tboil	368.70 ± 0.50	K	NIST
Tboil	370.34 ± 0.20	K	NIST
Tboil	369.80 ± 0.50	K	NIST
Tboil	370.40 ± 0.50	K	NIST
Tboil	370.40 ± 0.10	K	NIST
Tboil	369.20 ± 0.10	K	NIST
Tboil	369.30 ± 0.50	K	NIST
Tboil	369.90 ± 2.00	K	NIST
Tboil	369.75 ± 0.50	K	NIST
Tboil	371.00 ± 1.00	K	NIST
Tboil	371.00 ± 0.50	K	NIST
Tboil	370.60 ± 0.50	K	NIST
Tboil	370.56 ± 0.30	K	NIST
Tboil	Outlier 363.00 ± 4.00	K	NIST
Tc	[536.80; 537.00]	K
Tc	536.80	K	KDB
Tc	537.00	K	Measure...
Tc	537.00	K	Measure...
Tfus	[146.62; 147.00]	K
Tfus	147.00	K	KDB
Tfus	146.62	K	Aq. Sol...
Tfus	146.70	K	Phase e...
Tfus	146.95	K	NIST
Tfus	146.70 ± 0.50	K	NIST
Tfus	147.00 ± 3.00	K	NIST
Ttriple	[147.00; 148.75]	K
Ttriple	148.75	K	KDB
Ttriple	148.75 ± 0.02	K	NIST
Ttriple	148.75 ± 0.02	K	NIST
Ttriple	147.00 ± 0.30	K	NIST
Vc	[0.216; 0.218]	m3/kmol
Vc	0.218	m3/kmol	KDB
Vc	0.218	m3/kmol	NIST
Vc	0.216 ± 0.001	m3/kmol	NIST
Zc	0.2524720		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[102.26; 148.95]	J/mol×K	[371.20; 603.25]
Cp,gas	102.26 ± 0.20	J/mol×K	371.20	NIST
Cp,gas	107.28 ± 0.96	J/mol×K	375.45	NIST
Cp,gas	108.67 ± 0.96	J/mol×K	383.05	NIST
Cp,gas	109.42 ± 0.96	J/mol×K	387.15	NIST
Cp,gas	106.44 ± 0.21	J/mol×K	391.20	NIST
Cp,gas	111.21 ± 0.96	J/mol×K	396.95	NIST
Cp,gas	113.59 ± 0.96	J/mol×K	409.95	NIST
Cp,gas	110.42 ± 0.22	J/mol×K	411.20	NIST
Cp,gas	115.56 ± 0.96	J/mol×K	420.75	NIST
Cp,gas	115.97 ± 0.96	J/mol×K	422.95	NIST
Cp,gas	114.35 ± 0.23	J/mol×K	431.20	NIST
Cp,gas	118.71 ± 0.96	J/mol×K	437.95	NIST
Cp,gas	118.62 ± 0.24	J/mol×K	451.20	NIST
Cp,gas	122.94 ± 0.96	J/mol×K	461.05	NIST
Cp,gas	125.55 ± 0.96	J/mol×K	475.35	NIST
Cp,gas	130.97 ± 0.96	J/mol×K	504.95	NIST
Cp,gas	132.23 ± 0.96	J/mol×K	511.85	NIST
Cp,gas	135.98 ± 0.96	J/mol×K	532.35	NIST
Cp,gas	141.05 ± 0.96	J/mol×K	560.05	NIST
Cp,gas	144.49 ± 0.96	J/mol×K	578.85	NIST
Cp,gas	148.95 ± 0.96	J/mol×K	603.25	NIST
Cp,liquid	[131.30; 192.90]	J/mol×K	[270.00; 333.15]
Cp,liquid	136.00	J/mol×K	270.00	NIST
Cp,liquid	131.30	J/mol×K	274.60	NIST
Cp,liquid	133.50	J/mol×K	275.00	NIST
Cp,liquid	133.50	J/mol×K	275.40	NIST
Cp,liquid	139.00	J/mol×K	288.15	Excess ...
Cp,liquid	138.40	J/mol×K	288.15	NIST
Cp,liquid	142.30	J/mol×K	293.15	Excess ...
Cp,liquid	141.80	J/mol×K	293.15	NIST
Cp,liquid	144.60	J/mol×K	298.00	NIST
Cp,liquid	146.10	J/mol×K	298.00	NIST
Cp,liquid	144.80	J/mol×K	298.00	NIST
Cp,liquid	192.90	J/mol×K	298.10	NIST
Cp,liquid	145.60	J/mol×K	298.10	NIST
Cp,liquid	144.06	J/mol×K	298.15	NIST
Cp,liquid	144.44	J/mol×K	298.15	NIST
Cp,liquid	144.90	J/mol×K	298.15	Excess ...
Cp,liquid	146.88	J/mol×K	298.15	NIST
Cp,liquid	143.80	J/mol×K	298.15	NIST
Cp,liquid	143.96	J/mol×K	298.15	NIST
Cp,liquid	149.00	J/mol×K	298.15	NIST
Cp,liquid	143.78	J/mol×K	298.15	NIST
Cp,liquid	143.87	J/mol×K	298.15	NIST
Cp,liquid	143.77	J/mol×K	298.15	NIST
Cp,liquid	146.34	J/mol×K	298.22	NIST
Cp,liquid	164.80	J/mol×K	301.20	NIST
Cp,liquid	140.21	J/mol×K	303.00	NIST
Cp,liquid	148.20	J/mol×K	303.15	Excess ...
Cp,liquid	147.90	J/mol×K	303.40	NIST
Cp,liquid	151.00	J/mol×K	308.15	Excess ...
Cp,liquid	153.70	J/mol×K	313.15	Excess ...
Cp,liquid	158.60	J/mol×K	313.20	NIST
Cp,liquid	157.10	J/mol×K	318.15	Excess ...
Cp,liquid	155.60	J/mol×K	320.00	NIST
Cp,liquid	160.10	J/mol×K	323.15	Excess ...
Cp,liquid	164.50	J/mol×K	328.15	Excess ...
Cp,liquid	167.80	J/mol×K	333.15	Excess ...
Cp,solid	106.30	J/mol×K	150.00	NIST
η	[0.0005150; 0.0034744]	Pa×s	[283.15; 363.15]
η	0.0034744	Pa×s	283.15	Density...
η	0.0027676	Pa×s	288.15	Density...
η	0.0024202	Pa×s	288.15	Densiti...
η	0.0025070	Pa×s	288.15	Densiti...
η	0.0021900	Pa×s	293.00	Ultraso...
η	0.0022720	Pa×s	293.15	Densiti...
η	0.0021590	Pa×s	293.15	Viscosi...
η	0.0022050	Pa×s	293.15	Viscosi...
η	0.0021412	Pa×s	293.15	Densiti...
η	0.0022380	Pa×s	293.15	Density...
η	0.0021920	Pa×s	293.15	Densiti...
η	0.0021590	Pa×s	293.15	Dynamic...
η	0.0024104	Pa×s	293.15	Density...
η	0.0021940	Pa×s	293.15	Viscosi...
η	0.0021880	Pa×s	293.15	Density...
η	0.0021372	Pa×s	293.15	Densiti...
η	0.0022060	Pa×s	293.15	Propert...
η	0.0022020	Pa×s	293.15	Densiti...
η	0.0022040	Pa×s	293.15	Thermod...
η	0.0019400	Pa×s	298.15	Tempera...
η	0.0019550	Pa×s	298.15	Densiti...
η	0.0019430	Pa×s	298.15	Excess ...
η	0.0021178	Pa×s	298.15	Density...
η	0.0018939	Pa×s	298.15	Densiti...
η	0.0019660	Pa×s	298.15	Densiti...
η	0.0019500	Pa×s	298.15	Densiti...
η	0.0019150	Pa×s	298.15	Dynamic...
η	0.0019150	Pa×s	298.15	Viscosi...
η	0.0020420	Pa×s	298.15	Viscosi...
η	0.0019550	Pa×s	298.15	Densiti...
η	0.0019810	Pa×s	298.15	Density...
η	0.0019760	Pa×s	298.15	Propert...
η	0.0019450	Pa×s	298.15	Viscosi...
η	0.0019730	Pa×s	298.15	Densiti...
η	0.0019414	Pa×s	298.15	Densiti...
η	0.0016100	Pa×s	303.00	Ultraso...
η	0.0017140	Pa×s	303.15	Viscosi...
η	0.0017282	Pa×s	303.15	Densiti...
η	0.0016145	Pa×s	303.15	Thermod...
η	0.0017260	Pa×s	303.15	Densiti...
η	0.0017450	Pa×s	303.15	Density...
η	0.0017250	Pa×s	303.15	Excess ...
η	0.0017370	Pa×s	303.15	Propert...
η	0.0017370	Pa×s	303.15	Densiti...
η	0.0018742	Pa×s	303.15	Density...
η	0.0017325	Pa×s	303.15	Densiti...
η	0.0017330	Pa×s	303.15	Densiti...
η	0.0017880	Pa×s	303.15	Densiti...
η	0.0017190	Pa×s	303.15	Densiti...
η	0.0017130	Pa×s	303.15	Viscosi...
η	0.0016841	Pa×s	303.15	Densiti...
η	0.0017300	Pa×s	303.15	Viscosi...
η	0.0017130	Pa×s	303.15	Density...
η	0.0017130	Pa×s	303.15	Dynamic...
η	0.0015380	Pa×s	308.15	Densiti...
η	0.0015037	Pa×s	308.15	Densiti...
η	0.0015448	Pa×s	308.15	Densiti...
η	0.0015330	Pa×s	308.15	Densiti...
η	0.0015344	Pa×s	308.15	Densiti...
η	0.0016709	Pa×s	308.15	Density...
η	0.0015400	Pa×s	308.15	Tempera...
η	0.0015480	Pa×s	308.15	Propert...
η	0.0015650	Pa×s	308.15	Viscosi...
η	0.0015370	Pa×s	308.15	Excess ...
η	0.0015480	Pa×s	308.15	Densiti...
η	0.0013400	Pa×s	313.00	Ultraso...
η	0.0013840	Pa×s	313.15	Densiti...
η	0.0013810	Pa×s	313.15	Densiti...
η	0.0013516	Pa×s	313.15	Densiti...
η	0.0011883	Pa×s	313.15	Thermod...
η	0.0013672	Pa×s	313.15	Densiti...
η	0.0013847	Pa×s	313.15	Densiti...
η	0.0013830	Pa×s	313.15	Propert...
η	0.0013907	Pa×s	313.15	Densiti...
η	0.0013730	Pa×s	313.15	Densiti...
η	0.0013780	Pa×s	313.15	Density...
η	0.0013630	Pa×s	313.15	Densiti...
η	0.0015237	Pa×s	313.15	Density...
η	0.0013820	Pa×s	313.15	Viscosi...
η	0.0013810	Pa×s	313.15	Density...
η	0.0012410	Pa×s	318.15	Densiti...
η	0.0012340	Pa×s	318.15	Densiti...
η	0.0013833	Pa×s	318.15	Density...
η	0.0012240	Pa×s	318.15	Densiti...
η	0.0012400	Pa×s	318.15	Tempera...
η	0.0008796	Pa×s	323.15	Thermod...
η	0.0012560	Pa×s	323.15	Density...
η	0.0011050	Pa×s	323.15	Viscosi...
η	0.0011150	Pa×s	323.15	Density...
η	0.0011170	Pa×s	323.15	Densiti...
η	0.0011004	Pa×s	323.15	Densiti...
η	0.0011020	Pa×s	323.15	Densiti...
η	0.0010977	Pa×s	323.15	Densiti...
η	0.0010200	Pa×s	328.15	Tempera...
η	0.0011523	Pa×s	328.15	Density...
η	0.0009860	Pa×s	328.15	Densiti...
η	0.0009070	Pa×s	333.15	Density...
η	0.0008980	Pa×s	333.15	Densiti...
η	0.0010819	Pa×s	333.15	Density...
η	0.0005985	Pa×s	333.15	Thermod...
η	0.0008420	Pa×s	338.15	Tempera...
η	0.0008010	Pa×s	338.15	Densiti...
η	0.0007420	Pa×s	343.15	Density...
η	0.0007100	Pa×s	348.15	Tempera...
η	0.0006150	Pa×s	353.15	Density...
η	0.0005150	Pa×s	363.15	Density...
ΔfusH	[5.19; 5.40]	kJ/mol	[147.00; 148.80]
ΔfusH	5.19	kJ/mol	147.00	NIST
ΔfusH	5.40	kJ/mol	148.70	NIST
ΔfusH	5.37	kJ/mol	148.75	NIST
ΔfusH	5.37	kJ/mol	148.80	NIST
ΔfusH	5.37	kJ/mol	148.80	NIST
ΔvapH	[11.40; 49.30]	kJ/mol	[214.00; 528.00]
ΔvapH	48.00	kJ/mol	214.00	NIST
ΔvapH	46.40 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	46.70	kJ/mol	318.00	NIST
ΔvapH	45.70 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	49.30	kJ/mol	324.00	NIST
ΔvapH	46.90	kJ/mol	331.00	NIST
ΔvapH	44.90 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	44.99 ± 0.42	kJ/mol	333.13	NIST
ΔvapH	47.00	kJ/mol	336.50	NIST
ΔvapH	43.90 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	44.00 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	45.50	kJ/mol	344.00	NIST
ΔvapH	43.20 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	43.20	kJ/mol	354.00	NIST
ΔvapH	44.70	kJ/mol	355.00	NIST
ΔvapH	44.30	kJ/mol	358.00	NIST
ΔvapH	42.30 ± 0.10	kJ/mol	360.00	NIST
ΔvapH	42.40 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	44.10	kJ/mol	364.00	NIST
ΔvapH	43.50	kJ/mol	366.00	NIST
ΔvapH	42.90	kJ/mol	368.50	NIST
ΔvapH	41.20 ± 0.10	kJ/mol	370.00	NIST
ΔvapH	41.44	kJ/mol	370.30	NIST
ΔvapH	41.76	kJ/mol	370.40	KDB
ΔvapH	41.20	kJ/mol	371.00	NIST
ΔvapH	40.30 ± 0.10	kJ/mol	378.00	NIST
ΔvapH	39.70 ± 0.10	kJ/mol	384.00	NIST
ΔvapH	42.30	kJ/mol	388.00	NIST
ΔvapH	35.20	kJ/mol	423.00	NIST
ΔvapH	40.10	kJ/mol	441.50	NIST
ΔvapH	29.40	kJ/mol	453.00	NIST
ΔvapH	40.70	kJ/mol	471.00	NIST
ΔvapH	36.50	kJ/mol	492.50	NIST
ΔvapH	21.00	kJ/mol	498.00	NIST
ΔvapH	11.40	kJ/mol	528.00	NIST
Pvap	[0.70; 3546.00]	kPa	[278.15; 513.15]
Pvap	0.70	kPa	278.15	Vapor P...
Pvap	1.01	kPa	283.15	Vapor P...
Pvap	1.45	kPa	288.15	Vapor P...
Pvap	2.04	kPa	293.15	Vapor P...
Pvap	2.03	kPa	293.15	Thermod...
Pvap	2.88	kPa	298.15	Vapor-P...
Pvap	2.84	kPa	298.15	Vapor P...
Pvap	2.81	kPa	298.15	Thermod...
Pvap	2.79	kPa	298.15	Thermod...
Pvap	3.83	kPa	303.15	Thermod...
Pvap	4.00	kPa	303.15	Vapor-P...
Pvap	3.87	kPa	303.15	Vapor P...
Pvap	3.88	kPa	303.15	Thermod...
Pvap	3.63	kPa	303.15	Isother...
Pvap	5.23	kPa	308.15	Vapor P...
Pvap	5.25	kPa	308.15	Thermod...
Pvap	5.37	kPa	308.15	Vapor-P...
Pvap	5.20	kPa	308.15	Thermod...
Pvap	5.88	kPa	310.17	Vapor-L...
Pvap	6.99	kPa	313.15	Thermod...
Pvap	7.03	kPa	313.15	Thermod...
Pvap	7.01	kPa	313.15	Vapor P...
Pvap	6.98	kPa	313.15	Vapor-L...
Pvap	7.20	kPa	313.15	Vapor-P...
Pvap	6.99	kPa	313.17	P-x dat...
Pvap	7.69	kPa	314.84	Vapor-L...
Pvap	9.57	kPa	318.15	Vapor-P...
Pvap	9.01	kPa	318.15	Isother...
Pvap	9.29	kPa	318.15	Vapor P...
Pvap	9.31	kPa	318.15	Thermod...
Pvap	9.47	kPa	318.58	Vapor-L...
Pvap	10.00	kPa	319.65	P, rho,...
Pvap	10.18	kPa	319.89	Vapor-L...
Pvap	12.07	kPa	323.07	Vapor-L...
Pvap	12.18	kPa	323.15	Vapor P...
Pvap	12.32	kPa	323.15	Vapor-L...
Pvap	12.42	kPa	323.15	Vapor-P...
Pvap	12.27	kPa	323.26	Vapor-L...
Pvap	13.14	kPa	324.71	Vapor-L...
Pvap	15.00	kPa	327.25	P, rho,...
Pvap	15.75	kPa	328.14	Vapor-L...
Pvap	16.14	kPa	328.15	Vapor-P...
Pvap	17.57	kPa	330.16	Vapor-L...
Pvap	19.07	kPa	331.92	Vapor-L...
Pvap	19.17	kPa	332.05	Vapor-L...
Pvap	19.31	kPa	332.18	Vapor-L...
Pvap	20.00	kPa	332.95	P, rho,...
Pvap	20.72	kPa	333.15	Vapor-P...
Pvap	19.93	kPa	333.15	Isother...
Pvap	20.27	kPa	333.15	Vapor-L...
Pvap	21.90	kPa	334.53	Phase e...
Pvap	22.56	kPa	335.34	Vapor-L...
Pvap	25.00	kPa	337.45	P, rho,...
Pvap	25.60	kPa	337.95	Isobari...
Pvap	26.41	kPa	338.15	Vapor-P...
Pvap	26.91	kPa	339.01	Vapor-L...
Pvap	30.00	kPa	341.25	P, rho,...
Pvap	30.10	kPa	341.35	Isobari...
Pvap	31.20	kPa	342.07	Phase e...
Pvap	31.12	kPa	342.11	Vapor-L...
Pvap	31.45	kPa	342.83	P-x dat...
Pvap	33.23	kPa	343.15	Vapor-P...
Pvap	33.33	kPa	343.55	P, rho,...
Pvap	35.00	kPa	344.65	P, rho,...
Pvap	35.82	kPa	345.18	Vapor-L...
Pvap	37.40	kPa	346.15	Isobari...
Pvap	40.00	kPa	347.55	Isobari...
Pvap	40.00	kPa	347.65	P, rho,...
Pvap	40.12	kPa	347.71	Vapor-L...
Pvap	41.63	kPa	348.15	Vapor-P...
Pvap	42.90	kPa	349.12	Phase e...
Pvap	44.26	kPa	349.93	Vapor-L...
Pvap	45.00	kPa	350.35	P, rho,...
Pvap	46.00	kPa	350.80	Isobari...
Pvap	49.36	kPa	352.44	Vapor-L...
Pvap	49.80	kPa	352.68	P-x dat...
Pvap	50.00	kPa	352.75	P, rho,...
Pvap	51.67	kPa	353.15	Vapor-P...
Pvap	50.95	kPa	353.15	Vapor-L...
Pvap	50.95	kPa	353.17	Vapor-L...
Pvap	51.10	kPa	353.25	Isobari...
Pvap	52.70	kPa	353.96	Phase e...
Pvap	53.33	kPa	354.18	Isobari...
Pvap	55.00	kPa	355.05	P, rho,...
Pvap	59.13	kPa	356.70	Vapor-L...
Pvap	60.00	kPa	357.05	P, rho,...
Pvap	60.00	kPa	357.10	Isobari...
Pvap	60.70	kPa	357.35	Isobari...
Pvap	62.40	kPa	357.95	Phase e...
Pvap	63.69	kPa	358.15	Vapor-P...
Pvap	65.00	kPa	359.05	P, rho,...
Pvap	66.66	kPa	359.56	Isobari...
Pvap	66.66	kPa	359.65	P, rho,...
Pvap	70.00	kPa	360.85	P, rho,...
Pvap	71.40	kPa	361.25	Phase e...
Pvap	74.70	kPa	362.45	Isobari...
Pvap	75.00	kPa	362.55	P, rho,...
Pvap	77.81	kPa	363.15	Vapor-P...
Pvap	76.56	kPa	363.20	(Vapour...
Pvap	79.99	kPa	364.11	Isobari...
Pvap	80.00	kPa	364.15	P, rho,...
Pvap	80.00	kPa	364.20	Isobari...
Pvap	80.70	kPa	364.30	Phase e...
Pvap	81.30	kPa	364.51	Isother...
Pvap	81.20	kPa	364.53	Vapor L...
Pvap	85.00	kPa	365.65	P, rho,...
Pvap	86.80	kPa	366.25	Isobari...
Pvap	90.00	kPa	367.15	P, rho,...
Pvap	91.60	kPa	367.51	Phase e...
Pvap	93.32	kPa	368.08	Isobari...
Pvap	98.66	kPa	369.55	Isobari...
Pvap	100.00	kPa	369.80	Isobari...
Pvap	100.00	kPa	370.00	Isobari...
Pvap	101.33	kPa	370.05	P, rho,...
Pvap	100.51	kPa	370.10	Vapor-L...
Pvap	101.00	kPa	370.20	Heterog...
Pvap	101.30	kPa	370.33	Isobari...
Pvap	101.30	kPa	370.35	Isobari...
Pvap	101.30	kPa	370.40	Evaluat...
Pvap	101.80	kPa	370.40	Isobari...
Pvap	102.70	kPa	370.44	Phase e...
Pvap	114.90	kPa	373.65	Isobari...
Pvap	125.86	kPa	376.30	Vapor-L...
Pvap	151.03	kPa	381.50	Vapor-L...
Pvap	160.40	kPa	383.20	High-te...
Pvap	176.20	kPa	385.89	Vapor-L...
Pvap	201.37	kPa	389.89	Vapor-L...
Pvap	223.30	kPa	393.20	High-te...
Pvap	226.54	kPa	393.59	Vapor-L...
Pvap	251.71	kPa	396.19	Vapor-L...
Pvap	303.10	kPa	403.20	High-te...
Pvap	406.60	kPa	413.20	High-te...
Pvap	546.10	kPa	423.20	High-te...
Pvap	600.00	kPa	427.20	Experim...
Pvap	1558.00	kPa	468.15	Vapor-L...
Pvap	2081.00	kPa	483.15	Vapor-L...
Pvap	2733.00	kPa	498.15	Vapor-L...
Pvap	3546.00	kPa	513.15	Vapor-L...
n0	[1.37015; 1.38906]		[283.15; 328.15]
n0	1.38906		283.15	Thermop...
n0	1.38780		288.15	Experim...
n0	1.38690		288.15	Excess ...
n0	1.38785		288.15	Experim...
n0	1.38578		293.15	Experim...
n0	1.38500		293.15	Phase e...
n0	1.38480		293.15	Isother...
n0	1.38512		293.15	Vapor L...
n0	1.38550		293.15	Limitin...
n0	1.38530		293.15	Isother...
n0	1.38520		293.15	Solid-L...
n0	1.38432		293.15	Separat...
n0	1.38552		293.15	Excess ...
n0	1.38520		293.15	P-rho-T...
n0	1.38576		293.15	Experim...
n0	1.38510		293.15	Isobari...
n0	1.38200		293.15	Isother...
n0	1.38540		293.15	Solubil...
n0	1.38510		293.15	Vapor L...
n0	1.38530		293.15	Measure...
n0	1.38510		293.20	Vapor L...
n0	1.38510		293.20	Vapor L...
n0	1.38540		295.15	Isobari...
n0	1.38340		298.00	Determi...
n0	1.38310		298.15	Physica...
n0	1.38307		298.15	Thermop...
n0	1.38260		298.15	Thermod...
n0	1.38309		298.15	Density...
n0	1.38288		298.15	Thermop...
n0	1.38305		298.15	Experim...
n0	1.38260		298.15	Thermod...
n0	1.38220		298.15	Applica...
n0	1.38307		298.15	Effect ...
n0	1.38360		298.15	Liquid ...
n0	1.38400		298.15	Physico...
n0	1.38340		298.15	Excess ...
n0	1.38290		298.15	Experim...
n0	1.38340		298.15	Density...
n0	1.38330		298.15	Isother...
n0	1.38305		298.15	Liquid ...
n0	1.38300		298.15	Excess ...
n0	1.38560		298.15	Isobari...
n0	1.38334		298.15	Densiti...
n0	1.38320		298.15	Excess ...
n0	1.38330		298.15	Excess ...
n0	1.38360		298.15	Phase E...
n0	1.38330		298.15	Propert...
n0	1.38370		298.15	Experim...
n0	1.38369		298.15	Experim...
n0	1.38312		298.15	Isother...
n0	1.38305		298.15	Isobari...
n0	1.38364		298.15	Experim...
n0	1.38360		298.15	Isobari...
n0	1.38330		298.15	Effect ...
n0	1.38302		298.15	Physica...
n0	1.38330		298.15	Excess ...
n0	1.38304		298.15	Density...
n0	1.38350		298.15	Molar e...
n0	1.38333		298.15	Vapor l...
n0	1.38370		298.15	(Vapor ...
n0	1.38286		298.15	Effect ...
n0	1.38360		298.15	Phase e...
n0	1.38310		298.15	Synthes...
n0	1.38360		298.15	Vapor l...
n0	1.38360		298.15	Isobari...
n0	1.38070		298.15	Bubble ...
n0	1.38370		298.15	Activit...
n0	1.38290		298.15	Excess ...
n0	1.38300		298.15	Density...
n0	1.38306		298.15	Effect ...
n0	1.38308		298.15	Isobari...
n0	1.38390		298.20	Vapor l...
n0	1.38350		298.20	Measure...
n0	1.38190		303.15	Physico...
n0	1.38080		303.15	Thermod...
n0	1.38153		303.15	Experim...
n0	1.38080		303.15	Thermod...
n0	1.38210		303.15	Experim...
n0	1.38131		303.15	Densiti...
n0	1.38162		303.15	Experim...
n0	1.37820		308.15	Thermod...
n0	1.38000		308.15	Physico...
n0	1.37918		308.15	Experim...
n0	1.37929		308.15	Experim...
n0	1.37926		308.15	Densiti...
n0	1.37820		308.15	Thermod...
n0	1.37890		308.15	Excess ...
n0	1.37674		313.15	Thermop...
n0	1.37660		313.15	Thermop...
n0	1.37722		313.15	Densiti...
n0	1.37695		313.15	Experim...
n0	1.37702		313.15	Experim...
n0	1.37469		318.15	Experim...
n0	1.37483		318.15	Experim...
n0	1.37231		323.15	Experim...
n0	1.37252		323.15	Experim...
n0	1.37015		328.15	Thermop...
ρl	[742.77; 815.98]	kg/m3	[278.15; 363.15]
ρl	815.60	kg/m3	278.15	Thermop...
ρl	815.46	kg/m3	278.15	Density...
ρl	815.98	kg/m3	278.15	Volumet...
ρl	815.52	kg/m3	278.15	Density...
ρl	815.55	kg/m3	278.15	Thermod...
ρl	811.54	kg/m3	283.15	Excess ...
ρl	811.48	kg/m3	283.15	Densiti...
ρl	811.57	kg/m3	283.15	Volumet...
ρl	811.60	kg/m3	283.15	Thermod...
ρl	811.60	kg/m3	283.15	Density...
ρl	807.70	kg/m3	288.15	Thermop...
ρl	807.54	kg/m3	288.15	Volumet...
ρl	807.75	kg/m3	288.15	Experim...
ρl	807.62	kg/m3	288.15	Volumet...
ρl	807.75	kg/m3	288.15	Volumet...
ρl	807.50	kg/m3	288.15	Mass de...
ρl	807.83	kg/m3	288.15	Measure...
ρl	807.55	kg/m3	288.15	Excess ...
ρl	807.30	kg/m3	288.15	Tempera...
ρl	807.54	kg/m3	288.15	Densiti...
ρl	807.51	kg/m3	288.15	The exc...
ρl	807.64	kg/m3	288.15	Thermod...
ρl	809.01	kg/m3	288.15	Excess ...
ρl	807.86	kg/m3	288.15	Densiti...
ρl	807.69	kg/m3	288.15	Influen...
ρl	807.55	kg/m3	288.15	Thermop...
ρl	807.63	kg/m3	288.15	Density...
ρl	807.90	kg/m3	288.15	Thermod...
ρl	803.50	kg/m3	293.00	Fluid-P...
ρl	804.00	kg/m3	293.00	KDB
ρl	803.50	kg/m3	293.00	Fluid-P...
ρl	800.03	kg/m3	293.15	Excess ...
ρl	803.77	kg/m3	293.15	Volumet...
ρl	803.53	kg/m3	293.15	Volume ...
ρl	803.70	kg/m3	293.15	Influen...
ρl	803.52	kg/m3	293.15	The exc...
ρl	803.59	kg/m3	293.15	Excess ...
ρl	804.97	kg/m3	293.15	Densiti...
ρl	803.70	kg/m3	293.15	Measure...
ρl	803.65	kg/m3	293.15	Densiti...
ρl	803.86	kg/m3	293.15	Densiti...
ρl	803.52	kg/m3	293.15	Measure...
ρl	803.30	kg/m3	293.15	Excess ...
ρl	803.58	kg/m3	293.15	Densiti...
ρl	803.63	kg/m3	293.15	Excess ...
ρl	803.67	kg/m3	293.15	Volumet...
ρl	804.00	kg/m3	293.15	Composi...
ρl	803.62	kg/m3	293.15	Thermod...
ρl	804.14	kg/m3	293.15	Molecul...
ρl	803.59	kg/m3	293.15	Volumet...
ρl	803.85	kg/m3	293.15	(Liquid...
ρl	803.52	kg/m3	293.15	Electro...
ρl	803.75	kg/m3	293.15	Propert...
ρl	803.63	kg/m3	293.15	Volumet...
ρl	803.77	kg/m3	293.15	Experim...
ρl	803.85	kg/m3	293.15	(Liquid...
ρl	803.60	kg/m3	293.15	Liquid ...
ρl	803.57	kg/m3	293.15	Density...
ρl	803.61	kg/m3	293.15	Densiti...
ρl	803.66	kg/m3	293.15	Thermod...
ρl	803.76	kg/m3	293.15	Intermo...
ρl	803.00	kg/m3	293.15	Density...
ρl	803.71	kg/m3	293.15	Densiti...
ρl	803.65	kg/m3	293.15	Density...
ρl	803.77	kg/m3	293.15	Volumet...
ρl	803.60	kg/m3	293.15	Three B...
ρl	803.50	kg/m3	293.15	Density...
ρl	803.56	kg/m3	293.15	Densiti...
ρl	803.92	kg/m3	293.15	Osmotic...
ρl	803.49	kg/m3	293.15	Densiti...
ρl	803.84	kg/m3	293.15	Volumet...
ρl	803.48	kg/m3	293.15	Speed o...
ρl	799.50	kg/m3	298.00	Fluid-P...
ρl	800.00	kg/m3	298.00	Compara...
ρl	799.50	kg/m3	298.00	Fluid-P...
ρl	801.01	kg/m3	298.15	Densiti...
ρl	799.45	kg/m3	298.15	Apparen...
ρl	799.40	kg/m3	298.15	Excess ...
ρl	799.53	kg/m3	298.15	Volume ...
ρl	799.75	kg/m3	298.15	Measure...
ρl	799.50	kg/m3	298.15	Dynamic...
ρl	799.67	kg/m3	298.15	Volumet...
ρl	799.60	kg/m3	298.15	Densiti...
ρl	799.71	kg/m3	298.15	Densiti...
ρl	799.40	kg/m3	298.15	Density...
ρl	800.97	kg/m3	298.15	Excess ...
ρl	799.59	kg/m3	298.15	Excess ...
ρl	799.60	kg/m3	298.15	Vapor-L...
ρl	799.65	kg/m3	298.15	Density...
ρl	799.87	kg/m3	298.15	Physica...
ρl	797.60	kg/m3	298.15	Volumet...
ρl	804.27	kg/m3	298.15	Phase E...
ρl	799.56	kg/m3	298.15	ACSExce...
ρl	799.66	kg/m3	298.15	Thermod...
ρl	799.52	kg/m3	298.15	Separat...
ρl	799.70	kg/m3	298.15	Excess ...
ρl	799.52	kg/m3	298.15	Effect ...
ρl	799.52	kg/m3	298.15	Extract...
ρl	799.40	kg/m3	298.15	Tempera...
ρl	800.13	kg/m3	298.15	Molecul...
ρl	799.78	kg/m3	298.15	Densiti...
ρl	799.67	kg/m3	298.15	Thermop...
ρl	799.50	kg/m3	298.15	Isobari...
ρl	799.56	kg/m3	298.15	A combi...
ρl	799.54	kg/m3	298.15	Volumet...
ρl	799.60	kg/m3	298.15	Bubble ...
ρl	799.71	kg/m3	298.15	Propert...
ρl	799.65	kg/m3	298.15	FT-IR s...
ρl	799.60	kg/m3	298.15	Measure...
ρl	799.74	kg/m3	298.15	(Vapor ...
ρl	799.56	kg/m3	298.15	Excess ...
ρl	799.56	kg/m3	298.15	Measure...
ρl	799.70	kg/m3	298.15	Solubil...
ρl	799.85	kg/m3	298.15	Volumet...
ρl	799.61	kg/m3	298.15	Experim...
ρl	800.06	kg/m3	298.15	Solid-l...
ρl	799.62	kg/m3	298.15	Thermod...
ρl	802.00	kg/m3	298.15	Isobari...
ρl	800.94	kg/m3	298.15	Volumet...
ρl	800.10	kg/m3	298.15	Composi...
ρl	799.50	kg/m3	298.15	Fully a...
ρl	799.69	kg/m3	298.15	Physica...
ρl	799.93	kg/m3	298.15	A syste...
ρl	799.59	kg/m3	298.15	Densiti...
ρl	799.52	kg/m3	298.15	Separat...
ρl	799.53	kg/m3	298.15	Mass de...
ρl	799.67	kg/m3	298.15	Densiti...
ρl	799.71	kg/m3	298.15	Measure...
ρl	799.62	kg/m3	298.15	Liquid ...
ρl	799.58	kg/m3	298.15	Excess ...
ρl	800.13	kg/m3	298.15	Thermod...
ρl	799.56	kg/m3	298.15	Thermop...
ρl	800.61	kg/m3	298.15	Isother...
ρl	799.70	kg/m3	298.15	Thermod...
ρl	799.96	kg/m3	298.15	Liquid ...
ρl	799.67	kg/m3	298.15	Thermod...
ρl	799.70	kg/m3	298.15	Thermop...
ρl	799.49	kg/m3	298.15	Densiti...
ρl	799.76	kg/m3	298.15	Volumet...
ρl	799.55	kg/m3	298.15	Density...
ρl	799.69	kg/m3	298.15	Influen...
ρl	799.96	kg/m3	298.15	Tempera...
ρl	801.08	kg/m3	298.15	Modifie...
ρl	799.51	kg/m3	298.15	The exc...
ρl	799.65	kg/m3	298.15	Excess ...
ρl	799.46	kg/m3	298.15	Thermop...
ρl	799.70	kg/m3	298.15	Thermod...
ρl	799.52	kg/m3	298.15	Densiti...
ρl	799.94	kg/m3	298.15	Liquid ...
ρl	799.98	kg/m3	298.15	Binary ...
ρl	799.62	kg/m3	298.15	Volumet...
ρl	799.75	kg/m3	298.15	Experim...
ρl	799.89	kg/m3	298.15	Binary ...
ρl	799.51	kg/m3	298.15	Fluid P...
ρl	797.81	kg/m3	298.15	Excess ...
ρl	799.60	kg/m3	298.15	Experim...
ρl	799.28	kg/m3	298.15	Topolog...
ρl	799.81	kg/m3	298.15	Densiti...
ρl	800.61	kg/m3	298.15	Binary ...
ρl	799.70	kg/m3	298.15	Solubil...
ρl	799.65	kg/m3	298.15	Thermod...
ρl	799.28	kg/m3	298.15	Topolog...
ρl	799.30	kg/m3	298.15	Thermod...
ρl	800.70	kg/m3	298.15	Apparen...
ρl	799.10	kg/m3	298.15	Excess ...
ρl	799.51	kg/m3	298.15	Excess ...
ρl	799.74	kg/m3	298.15	Densiti...
ρl	799.97	kg/m3	298.15	Excess ...
ρl	799.69	kg/m3	298.15	Volumet...
ρl	800.62	kg/m3	298.15	Speeds ...
ρl	800.00	kg/m3	298.15	Density...
ρl	799.52	kg/m3	298.15	Electro...
ρl	799.56	kg/m3	298.15	Refract...
ρl	799.47	kg/m3	298.15	Speed o...
ρl	799.92	kg/m3	298.20	A green...
ρl	796.00	kg/m3	303.00	Compara...
ρl	795.50	kg/m3	303.00	Fluid-P...
ρl	795.50	kg/m3	303.00	Fluid-P...
ρl	795.55	kg/m3	303.15	Excess ...
ρl	796.55	kg/m3	303.15	Isother...
ρl	796.89	kg/m3	303.15	Densiti...
ρl	795.72	kg/m3	303.15	Experim...
ρl	795.58	kg/m3	303.15	Volumet...
ρl	796.00	kg/m3	303.15	Density...
ρl	795.53	kg/m3	303.15	Vapor-l...
ρl	795.65	kg/m3	303.15	Influen...
ρl	795.72	kg/m3	303.15	Volumet...
ρl	795.82	kg/m3	303.15	Intermo...
ρl	795.48	kg/m3	303.15	Excess ...
ρl	795.87	kg/m3	303.15	Densiti...
ρl	795.61	kg/m3	303.15	Volumet...
ρl	795.62	kg/m3	303.15	Thermod...
ρl	795.70	kg/m3	303.15	Measure...
ρl	795.47	kg/m3	303.15	Measure...
ρl	795.05	kg/m3	303.15	Excess ...
ρl	796.00	kg/m3	303.15	Composi...
ρl	795.89	kg/m3	303.15	A syste...
ρl	795.81	kg/m3	303.15	Volumet...
ρl	795.50	kg/m3	303.15	Electro...
ρl	795.53	kg/m3	303.15	Density...
ρl	795.57	kg/m3	303.15	Densiti...
ρl	795.50	kg/m3	303.15	Densiti...
ρl	795.53	kg/m3	303.15	Volumet...
ρl	795.58	kg/m3	303.15	Volumet...
ρl	796.40	kg/m3	303.15	Excess ...
ρl	795.10	kg/m3	303.15	Excess ...
ρl	795.49	kg/m3	303.15	Volume ...
ρl	795.70	kg/m3	303.15	Liquid ...
ρl	795.40	kg/m3	303.15	Density...
ρl	795.58	kg/m3	303.15	Densiti...
ρl	795.65	kg/m3	303.15	FT-IR s...
ρl	795.48	kg/m3	303.15	The exc...
ρl	795.61	kg/m3	303.15	Density...
ρl	795.94	kg/m3	303.15	Physica...
ρl	798.00	kg/m3	303.15	Study o...
ρl	795.92	kg/m3	303.15	Tempera...
ρl	796.08	kg/m3	303.15	Molecul...
ρl	795.80	kg/m3	303.15	Viscous...
ρl	795.58	kg/m3	303.15	Thermod...
ρl	795.54	kg/m3	303.15	Isobari...
ρl	795.77	kg/m3	303.15	Densiti...
ρl	795.58	kg/m3	303.15	Densiti...
ρl	795.46	kg/m3	303.15	Densiti...
ρl	795.65	kg/m3	303.15	Propert...
ρl	795.54	kg/m3	303.15	Densiti...
ρl	795.44	kg/m3	303.15	Speed o...
ρl	792.00	kg/m3	308.00	Compara...
ρl	791.58	kg/m3	308.15	Influen...
ρl	791.43	kg/m3	308.15	Volume ...
ρl	791.76	kg/m3	308.15	Thermod...
ρl	791.46	kg/m3	308.15	Thermop...
ρl	791.43	kg/m3	308.15	Electro...
ρl	791.80	kg/m3	308.15	Densiti...
ρl	791.83	kg/m3	308.15	Densiti...
ρl	791.69	kg/m3	308.15	Densiti...
ρl	791.55	kg/m3	308.15	Thermod...
ρl	791.30	kg/m3	308.15	Density...
ρl	791.74	kg/m3	308.15	Volumet...
ρl	791.39	kg/m3	308.15	Densiti...
ρl	791.60	kg/m3	308.15	Thermop...
ρl	791.53	kg/m3	308.15	Densiti...
ρl	791.36	kg/m3	308.15	Thermop...
ρl	791.30	kg/m3	308.15	Tempera...
ρl	791.44	kg/m3	308.15	Volumet...
ρl	791.84	kg/m3	308.15	Osmotic...
ρl	791.63	kg/m3	308.15	Measure...
ρl	791.71	kg/m3	308.15	Densiti...
ρl	791.49	kg/m3	308.15	Volumet...
ρl	791.82	kg/m3	308.15	Tempera...
ρl	791.64	kg/m3	308.15	Volumet...
ρl	791.52	kg/m3	308.15	Volumet...
ρl	791.82	kg/m3	308.15	A syste...
ρl	791.50	kg/m3	308.15	Densiti...
ρl	792.76	kg/m3	308.15	Physica...
ρl	791.64	kg/m3	308.15	Experim...
ρl	791.47	kg/m3	308.15	Excess ...
ρl	791.54	kg/m3	308.15	Density...
ρl	791.51	kg/m3	308.15	Thermod...
ρl	791.42	kg/m3	308.15	The exc...
ρl	791.65	kg/m3	308.15	FT-IR s...
ρl	791.56	kg/m3	308.15	Propert...
ρl	791.40	kg/m3	308.15	Measure...
ρl	791.44	kg/m3	308.15	Mass de...
ρl	792.83	kg/m3	308.15	Densiti...
ρl	791.78	kg/m3	308.15	Physica...
ρl	792.00	kg/m3	308.15	Molecul...
ρl	791.40	kg/m3	308.15	Vapor-L...
ρl	791.37	kg/m3	308.15	Speed o...
ρl	789.00	kg/m3	313.00	Compara...
ρl	787.30	kg/m3	313.15	Measure...
ρl	787.36	kg/m3	313.15	Excess ...
ρl	787.88	kg/m3	313.15	Molecul...
ρl	787.31	kg/m3	313.15	The exc...
ρl	787.42	kg/m3	313.15	Propert...
ρl	787.39	kg/m3	313.15	Densiti...
ρl	787.41	kg/m3	313.15	Thermod...
ρl	787.43	kg/m3	313.15	Density...
ρl	787.52	kg/m3	313.15	Measure...
ρl	787.35	kg/m3	313.15	Density...
ρl	788.00	kg/m3	313.15	Composi...
ρl	787.52	kg/m3	313.15	Volumet...
ρl	787.95	kg/m3	313.15	Excess ...
ρl	787.88	kg/m3	313.15	Intermo...
ρl	787.37	kg/m3	313.15	Volumet...
ρl	787.47	kg/m3	313.15	Influen...
ρl	788.00	kg/m3	313.15	Density...
ρl	787.73	kg/m3	313.15	Tempera...
ρl	787.38	kg/m3	313.15	Volumet...
ρl	787.44	kg/m3	313.15	Densiti...
ρl	788.69	kg/m3	313.15	Excess ...
ρl	787.20	kg/m3	313.15	Density...
ρl	789.07	kg/m3	313.15	Densiti...
ρl	787.29	kg/m3	313.15	Densiti...
ρl	787.30	kg/m3	313.15	Densiti...
ρl	787.83	kg/m3	313.15	Densiti...
ρl	787.50	kg/m3	313.15	Liquid ...
ρl	787.52	kg/m3	313.15	Experim...
ρl	787.32	kg/m3	313.15	Volume ...
ρl	787.36	kg/m3	313.15	Excess ...
ρl	787.00	kg/m3	313.15	Excess ...
ρl	787.64	kg/m3	313.15	Volumet...
ρl	788.60	kg/m3	313.15	Excess ...
ρl	787.31	kg/m3	313.15	Electro...
ρl	787.72	kg/m3	313.15	Densiti...
ρl	787.34	kg/m3	313.15	Densiti...
ρl	787.42	kg/m3	313.15	Volumet...
ρl	787.37	kg/m3	313.15	Densiti...
ρl	787.26	kg/m3	313.15	Speed o...
ρl	783.12	kg/m3	318.15	Measure...
ρl	783.16	kg/m3	318.15	Volume ...
ρl	783.30	kg/m3	318.15	Densiti...
ρl	783.36	kg/m3	318.15	Volumet...
ρl	783.10	kg/m3	318.15	Density...
ρl	783.12	kg/m3	318.15	Vapor-L...
ρl	783.27	kg/m3	318.15	Density...
ρl	783.15	kg/m3	318.15	The exc...
ρl	783.64	kg/m3	318.15	Densiti...
ρl	783.17	kg/m3	318.15	Volumet...
ρl	783.11	kg/m3	318.15	Electro...
ρl	783.36	kg/m3	318.15	Measure...
ρl	783.56	kg/m3	318.15	Densiti...
ρl	783.18	kg/m3	318.15	Density...
ρl	784.45	kg/m3	318.15	Physica...
ρl	783.22	kg/m3	318.15	Volumet...
ρl	783.10	kg/m3	318.15	Thermop...
ρl	783.30	kg/m3	318.15	Thermop...
ρl	783.16	kg/m3	318.15	Thermod...
ρl	783.22	kg/m3	318.15	Volumet...
ρl	783.86	kg/m3	318.15	Densiti...
ρl	783.30	kg/m3	318.15	Densiti...
ρl	783.20	kg/m3	318.15	Thermop...
ρl	783.20	kg/m3	318.15	Excess ...
ρl	783.18	kg/m3	318.15	Mass de...
ρl	783.36	kg/m3	318.15	Experim...
ρl	783.55	kg/m3	318.15	Volumet...
ρl	783.14	kg/m3	318.15	Densiti...
ρl	783.10	kg/m3	318.15	Speed o...
ρl	779.14	kg/m3	323.15	Volumet...
ρl	778.98	kg/m3	323.15	Density...
ρl	780.00	kg/m3	323.15	Composi...
ρl	779.11	kg/m3	323.15	Densiti...
ρl	779.14	kg/m3	323.15	Measure...
ρl	779.30	kg/m3	323.15	Liquid-...
ρl	779.02	kg/m3	323.15	Densiti...
ρl	779.01	kg/m3	323.15	Densiti...
ρl	778.92	kg/m3	323.15	Volumet...
ρl	779.01	kg/m3	323.15	Volumet...
ρl	780.74	kg/m3	323.15	Densiti...
ρl	778.93	kg/m3	323.15	Densiti...
ρl	779.33	kg/m3	323.15	Osmotic...
ρl	779.09	kg/m3	323.15	Osmotic...
ρl	779.05	kg/m3	323.15	Density...
ρl	778.79	kg/m3	323.15	Electro...
ρl	779.00	kg/m3	323.15	Densiti...
ρl	779.14	kg/m3	323.15	Experim...
ρl	778.97	kg/m3	323.15	Densiti...
ρl	778.93	kg/m3	323.15	Measure...
ρl	779.36	kg/m3	323.15	Densiti...
ρl	779.20	kg/m3	323.15	Liquid ...
ρl	778.70	kg/m3	323.15	Excess ...
ρl	778.90	kg/m3	323.15	Density...
ρl	778.96	kg/m3	323.15	Volumet...
ρl	779.09	kg/m3	323.15	Vapor-l...
ρl	779.32	kg/m3	323.15	Volumet...
ρl	780.00	kg/m3	323.15	Density...
ρl	778.90	kg/m3	323.15	Speed o...
ρl	774.90	kg/m3	328.15	Densiti...
ρl	774.70	kg/m3	328.15	Mass de...
ρl	774.63	kg/m3	328.15	Thermop...
ρl	774.86	kg/m3	328.15	Densiti...
ρl	774.73	kg/m3	328.15	Volumet...
ρl	775.97	kg/m3	328.15	Excess ...
ρl	774.72	kg/m3	328.15	Thermop...
ρl	774.90	kg/m3	328.15	Thermop...
ρl	774.79	kg/m3	328.15	Density...
ρl	770.54	kg/m3	333.15	Densiti...
ρl	770.39	kg/m3	333.15	Volumet...
ρl	770.44	kg/m3	333.15	Density...
ρl	770.38	kg/m3	333.15	Density...
ρl	771.75	kg/m3	333.15	Densiti...
ρl	764.00	kg/m3	333.15	Composi...
ρl	770.80	kg/m3	333.15	Densiti...
ρl	770.42	kg/m3	333.15	Densiti...
ρl	770.32	kg/m3	333.15	Measure...
ρl	770.42	kg/m3	333.15	Densiti...
ρl	765.98	kg/m3	338.15	Thermop...
ρl	766.20	kg/m3	338.15	Thermop...
ρl	765.96	kg/m3	338.15	Density...
ρl	766.03	kg/m3	338.15	Density...
ρl	766.15	kg/m3	338.15	Densiti...
ρl	761.51	kg/m3	343.15	Densiti...
ρl	761.53	kg/m3	343.15	Density...
ρl	761.67	kg/m3	343.15	Densiti...
ρl	762.86	kg/m3	343.15	Densiti...
ρl	756.91	kg/m3	348.15	Thermop...
ρl	757.09	kg/m3	348.15	Densiti...
ρl	752.44	kg/m3	353.15	Densiti...
ρl	747.65	kg/m3	358.15	Densiti...
ρl	742.77	kg/m3	363.15	Densiti...
ΔfusS	[35.30; 36.11]	J/mol×K	[147.00; 148.75]
ΔfusS	35.30	J/mol×K	147.00	NIST
ΔfusS	36.11	J/mol×K	148.75	NIST
csound,fluid	[1070.97; 1275.27]	m/s	[278.15; 338.15]
csound,fluid	1275.27	m/s	278.15	Volumet...
csound,fluid	1257.90	m/s	283.15	Excess ...
csound,fluid	1240.01	m/s	288.15	Densiti...
csound,fluid	1239.86	m/s	288.15	Volumet...
csound,fluid	1223.40	m/s	293.15	Acousti...
csound,fluid	1223.17	m/s	293.15	Densiti...
csound,fluid	1206.47	m/s	298.15	Densiti...
csound,fluid	1205.80	m/s	298.15	Ultraso...
csound,fluid	1207.00	m/s	298.15	Compres...
csound,fluid	1205.37	m/s	298.15	Volumet...
csound,fluid	1206.00	m/s	298.15	Excess ...
csound,fluid	1189.86	m/s	303.15	Densiti...
csound,fluid	1172.30	m/s	308.15	Acousti...
csound,fluid	1172.04	m/s	308.15	Densiti...
csound,fluid	1171.41	m/s	308.15	Volumet...
csound,fluid	1155.10	m/s	313.15	Excess ...
csound,fluid	1137.83	m/s	318.15	Volumet...
csound,fluid	1121.80	m/s	323.15	Acousti...
csound,fluid	1104.40	m/s	328.15	Volumet...
csound,fluid	1070.97	m/s	338.15	Volumet...
γ	[0.02; 0.02]	N/m	[278.15; 333.20]
γ	0.02	N/m	278.15	Applica...
γ	0.02	N/m	283.15	Applica...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	288.15	Applica...
γ	0.02	N/m	288.15	Study o...
γ	0.02	N/m	288.15	The mol...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.15	The mol...
γ	0.02	N/m	293.15	Applica...
γ	0.02	N/m	293.20	Surface...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.00	Surface...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Study o...
γ	0.02	N/m	298.15	Applica...
γ	0.02	N/m	298.15	The mol...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	303.15	Applica...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	The mol...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.20	Surface...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Applica...
γ	0.02	N/m	308.15	The mol...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Study o...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	313.15	The mol...
γ	0.02	N/m	313.15	Applica...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.20	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	The mol...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Study o...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.20	Surface...
γ	0.02	N/m	328.15	Study o...
γ	0.02	N/m	333.20	Surface...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[360.86; 423.16]	K	[69.79; 561.50]
Tboil	360.86	K	69.79	A novel...
Tboil	362.60	K	74.92	A novel...
Tboil	364.11	K	79.60	A novel...
Tboil	365.70	K	84.80	A novel...
Tboil	367.14	K	89.78	A novel...
Tboil	368.52	K	94.77	A novel...
Tboil	369.82	K	99.70	A novel...
Tboil	371.30	K	105.14	A novel...
Tboil	372.42	K	110.10	A novel...
Tboil	373.15	K	113.19	A novel...
Tboil	374.88	K	120.75	A novel...
Tboil	376.91	K	130.10	A novel...
Tboil	384.57	K	171.00	A novel...
Tboil	389.14	K	199.90	A novel...
Tboil	393.15	K	228.50	A novel...
Tboil	393.35	K	229.90	A novel...
Tboil	397.13	K	260.00	A novel...
Tboil	400.57	K	290.00	A novel...
Tboil	402.71	K	310.00	A novel...
Tboil	404.74	K	330.00	A novel...
Tboil	406.69	K	350.00	A novel...
Tboil	409.43	K	380.00	A novel...
Tboil	411.18	K	400.00	A novel...
Tboil	412.84	K	420.00	A novel...
Tboil	415.23	K	450.00	A novel...
Tboil	417.52	K	480.00	A novel...
Tboil	418.96	K	500.00	A novel...
Tboil	420.37	K	520.00	A novel...
Tboil	421.06	K	530.00	A novel...
Tboil	422.41	K	550.00	A novel...
Tboil	423.16	K	561.50	A novel...

Datasets

1. Molar heat capacity at constant volume, J/K/mol (1)
2. Viscosity, Pa*s (2)
3. Refractive index (Na D-line) (2)
4. Mass density, kg/m3 (12)
5. Speed of sound, m/s (3)
6. Molar volume, m3/mol (1)

Molar heat capacity at constant volume, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant volume, J/K/mol - Liquid
314.15	4353.00	130.947
315.15	5217.00	131.0071
316.15	6081.00	131.7283
317.15	6946.00	132.6297
318.15	7808.00	133.2307
319.15	8666.00	133.2908
320.15	9526.00	133.6513
321.15	10392.00	134.6128
322.15	11260.00	134.9133
323.15	12130.00	135.8147
324.15	13000.00	135.8748
325.15	13871.00	136.3556
326.15	14740.00	137.4974
327.15	15599.00	136.9566
328.15	16461.00	139.1801
329.15	17326.00	138.519
330.15	18193.00	138.6993
331.15	19066.00	139.9012
332.15	19945.00	139.6007
333.15	20825.00	140.1416
334.15	21705.00	140.8026
335.15	22585.00	141.4637
336.15	23467.00	141.644
337.15	24350.00	141.2834
338.15	25234.00	142.5454
339.15	26119.00	142.7858
340.15	27006.00	143.7473
341.15	27893.00	143.0862
342.15	28774.00	145.0093
343.15	3874.00	148.615
343.15	29657.00	143.9276
344.15	4675.00	146.9924
345.15	5478.00	149.3361
346.15	6283.00	148.1943
347.15	7088.00	149.5164
348.15	7896.00	148.8554
349.15	8704.00	149.9972
350.15	9514.00	150.7784
351.15	10326.00	149.9972
352.15	11138.00	151.3193
353.15	11953.00	151.7399
354.15	12769.00	152.4611
355.15	13587.00	151.6798
356.15	14406.00	152.5813
357.15	15227.00	152.9418
358.15	16050.00	153.4827
359.15	16870.00	153.4226
360.15	17670.00	155.3456
361.15	18489.00	154.1437
362.15	19314.00	155.5259
363.15	20144.00	154.9851
364.15	20977.00	154.9851
365.15	21811.00	155.4057
366.15	22647.00	156.6677
367.15	23484.00	156.0067
368.15	24324.00	156.0668
369.15	25165.00	156.9682
370.15	26008.00	156.3071
371.15	26853.00	157.0884
372.15	2876.00	161.3551
372.15	27699.00	156.5475
373.15	3622.00	161.9561
373.15	28548.00	157.5691
374.15	4369.00	162.1965
374.15	29398.00	157.8095
375.15	5118.00	162.4969
376.15	5868.00	163.158
377.15	6620.00	163.158
378.15	7374.00	162.8575
379.15	8129.00	163.2181
380.15	8887.00	163.6387
381.15	9646.00	163.7589
382.15	10407.00	162.8575
383.15	11170.00	164.6003
384.15	11935.00	162.7373
385.15	12702.00	164.4801
386.15	13470.00	163.819
387.15	14240.00	164.2397
388.15	15013.00	164.1796
389.15	15786.00	164.2998
390.15	16562.00	164.2397
391.15	17338.00	164.8406
392.15	18116.00	163.4585
393.15	18896.00	164.3599
394.15	19677.00	164.2998
395.15	20459.00	164.3599
396.15	21244.00	164.5402
397.15	22030.00	164.6604
398.15	22817.00	164.7204
399.15	23606.00	164.8406
400.15	24395.00	163.9993
401.15	25186.00	164.3599
402.15	25978.00	164.2397
403.15	26772.00	163.7589
404.15	27566.00	163.819
405.15	28362.00	163.0979
406.15	29159.00	163.5786
414.15	10151.00	171.2708
415.15	10841.00	173.7948
416.15	11533.00	172.5929
417.15	12227.00	172.7732
418.15	12922.00	173.0737
419.15	13618.00	171.6314
420.15	14316.00	172.5328
421.15	15015.00	172.2924
422.15	15715.00	172.052
423.15	16417.00	172.3525
424.15	17119.00	172.4126
427.15	19232.00	172.1121
428.15	19938.00	171.4511
429.15	20645.00	171.4511
430.15	21353.00	172.052
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0019
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
100.00	293.15	0.0022
100.00	313.15	0.0014
100.00	333.15	0.0009
100.00	353.15	0.0006
20000.00	293.15	0.0025
20000.00	313.15	0.0016
20000.00	333.15	0.0011
20000.00	353.15	0.0007
40000.00	293.15	0.0029
40000.00	313.15	0.0019
40000.00	333.15	0.0013
40000.00	353.15	0.0008
60000.00	293.15	0.0032
60000.00	313.15	0.0021
60000.00	333.15	0.0014
60000.00	353.15	0.0010
80000.00	293.15	0.0036
80000.00	313.15	0.0024
80000.00	333.15	0.0016
80000.00	353.15	0.0011
100000.00	293.15	0.0041
100000.00	313.15	0.0026
100000.00	333.15	0.0018
100000.00	353.15	0.0012
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
100.00	298.15	1.3836
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
294.15	100.00	1.3846
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	293.15	803.5
100.00	303.15	795.2
100.00	313.15	787.6
100.00	323.15	779.3
100.00	333.15	770.5
100.00	343.15	761.0
100.00	353.15	752.2
5000.00	293.15	807.3
5000.00	303.15	799.2
5000.00	313.15	791.9
5000.00	323.15	783.7
5000.00	333.15	775.4
5000.00	343.15	766.0
5000.00	353.15	757.6
10000.00	293.15	810.9
10000.00	303.15	802.9
10000.00	313.15	795.9
10000.00	323.15	788.0
10000.00	333.15	780.0
10000.00	343.15	770.7
10000.00	353.15	762.7
15000.00	293.15	814.3
15000.00	303.15	806.7
15000.00	313.15	799.7
15000.00	323.15	792.0
15000.00	333.15	784.3
15000.00	343.15	775.3
15000.00	353.15	767.6
20000.00	293.15	817.7
20000.00	303.15	810.1
20000.00	313.15	803.3
20000.00	323.15	795.8
20000.00	333.15	788.4
20000.00	343.15	779.6
20000.00	353.15	772.1
25000.00	293.15	821.0
25000.00	303.15	813.6
25000.00	313.15	806.8
25000.00	323.15	799.7
25000.00	333.15	792.0
25000.00	343.15	783.7
25000.00	353.15	776.3
30000.00	293.15	824.0
30000.00	303.15	816.7
30000.00	313.15	810.2
30000.00	323.15	803.2
30000.00	333.15	795.7
30000.00	343.15	787.6
30000.00	353.15	780.4
35000.00	293.15	827.0
35000.00	303.15	819.8
35000.00	313.15	813.5
35000.00	323.15	806.6
35000.00	333.15	799.2
35000.00	343.15	791.2
35000.00	353.15	784.1
40000.00	293.15	829.9
40000.00	303.15	822.9
40000.00	313.15	816.6
40000.00	323.15	809.9
40000.00	333.15	802.6
40000.00	343.15	794.7
40000.00	353.15	787.7
45000.00	293.15	832.7
45000.00	303.15	825.8
45000.00	313.15	819.7
45000.00	323.15	813.0
45000.00	333.15	805.9
45000.00	343.15	798.3
45000.00	353.15	791.8
50000.00	293.15	835.4
50000.00	303.15	828.8
50000.00	313.15	822.7
50000.00	323.15	816.1
50000.00	333.15	809.1
50000.00	343.15	801.6
50000.00	353.15	795.1
55000.00	293.15	838.1
55000.00	303.15	831.6
55000.00	313.15	825.5
55000.00	323.15	819.0
55000.00	333.15	812.3
55000.00	343.15	804.6
55000.00	353.15	798.5
60000.00	293.15	840.7
60000.00	303.15	834.2
60000.00	313.15	828.3
60000.00	323.15	821.8
60000.00	333.15	815.2
60000.00	343.15	807.7
60000.00	353.15	801.7
65000.00	293.15	843.2
65000.00	303.15	837.0
65000.00	313.15	831.0
65000.00	323.15	824.6
65000.00	333.15	818.1
65000.00	343.15	810.6
65000.00	353.15	805.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	110.00	799.54
298.15	5270.00	803.6
298.15	9870.00	807.01
298.15	14700.00	810.46
298.15	20530.00	814.46
298.15	25030.00	817.44
298.15	30100.00	820.7
298.15	35010.00	823.76
298.15	39560.00	826.52
323.15	590.00	779.78
323.15	5940.00	784.71
323.15	10600.00	788.81
323.15	16000.00	793.2
323.15	20640.00	796.73
323.15	24880.00	799.83
323.15	30800.00	803.99
323.15	35220.00	807.01
323.15	39790.00	810.02
348.15	140.00	757.11
348.15	5170.00	762.68
348.15	10260.00	767.5
348.15	15790.00	772.52
348.15	20560.00	776.41
348.15	24810.00	780.32
348.15	29300.00	784.09
348.15	35560.00	789.01
348.15	39950.00	792.23
373.15	360.00	733.24
373.15	5480.00	739.29
373.15	10290.00	745.11
373.15	15700.00	750.9
373.15	19960.00	755.19
373.15	25170.00	760.17
373.15	30510.00	765.02
373.15	35920.00	769.7
373.15	39780.00	772.91
398.15	620.00	705.55
398.15	5670.00	713.23
398.15	10620.00	720.1
398.15	15580.00	726.46
398.15	20350.00	732.35
398.15	25090.00	737.77
398.15	31150.00	744.07
398.15	35410.00	748.41
398.15	39390.00	752.32
423.15	1570.00	674.63
423.15	5870.00	682.79
423.15	10160.00	690.93
423.15	15320.00	699.32
423.15	20500.00	707.2
423.15	26280.00	715.01
423.15	31600.00	721.36
423.15	35780.00	726.03
423.15	39700.00	730.17
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	803.8
293.15	10000.00	811.3
293.15	20000.00	818.1
293.15	30000.00	824.4
293.15	40000.00	830.0
293.15	50000.00	835.6
293.15	60000.00	841.0
293.15	70000.00	845.9
293.15	80000.00	850.7
293.15	90000.00	855.2
293.15	100000.00	859.6
293.15	110000.00	863.7
293.15	120000.00	867.8
293.15	130000.00	871.6
293.15	140000.00	875.3
313.15	100.00	787.1
313.15	10000.00	795.5
313.15	20000.00	803.0
313.15	30000.00	810.0
313.15	40000.00	816.4
313.15	50000.00	822.3
313.15	60000.00	827.9
313.15	70000.00	833.2
313.15	80000.00	838.3
313.15	90000.00	843.0
313.15	100000.00	847.9
313.15	110000.00	852.3
313.15	120000.00	856.6
313.15	130000.00	860.7
313.15	140000.00	864.6
333.15	100.00	769.9
333.15	10000.00	780.0
333.15	20000.00	788.3
333.15	30000.00	795.7
333.15	40000.00	802.5
333.15	50000.00	809.0
333.15	60000.00	815.0
333.15	70000.00	820.6
333.15	80000.00	826.2
333.15	90000.00	831.2
333.15	100000.00	836.3
333.15	110000.00	840.9
333.15	120000.00	845.3
333.15	130000.00	849.6
333.15	140000.00	853.6
353.15	100.00	752.0
353.15	10000.00	762.5
353.15	20000.00	771.8
353.15	30000.00	780.2
353.15	40000.00	787.9
353.15	50000.00	795.0
353.15	60000.00	801.4
353.15	70000.00	807.7
353.15	80000.00	813.4
353.15	90000.00	818.7
353.15	100000.00	823.8
353.15	110000.00	828.8
353.15	120000.00	833.5
353.15	130000.00	837.9
353.15	140000.00	842.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	815.7
278.15	1000.00	816.4
278.15	5000.00	819.4
278.15	10000.00	822.8
278.15	15000.00	826.2
278.15	20000.00	829.4
278.15	25000.00	832.6
278.15	30000.00	835.7
278.15	35000.00	838.6
278.15	40000.00	841.5
278.15	45000.00	844.3
278.15	50000.00	847.1
278.15	55000.00	849.7
278.15	60000.00	852.1
288.15	100.00	807.8
288.15	1000.00	808.5
288.15	5000.00	811.6
288.15	10000.00	815.3
288.15	15000.00	818.9
288.15	20000.00	822.3
288.15	25000.00	825.5
288.15	30000.00	828.7
288.15	35000.00	831.8
288.15	40000.00	834.7
288.15	45000.00	837.6
288.15	50000.00	840.4
288.15	55000.00	843.1
288.15	60000.00	845.6
298.15	100.00	799.8
298.15	1000.00	800.5
298.15	5000.00	803.8
298.15	10000.00	807.6
298.15	15000.00	811.4
298.15	20000.00	814.9
298.15	25000.00	818.3
298.15	30000.00	821.6
298.15	35000.00	824.8
298.15	40000.00	827.9
298.15	45000.00	830.9
298.15	50000.00	833.8
298.15	55000.00	836.6
298.15	60000.00	839.2
308.15	100.00	791.6
308.15	1000.00	792.4
308.15	5000.00	795.8
308.15	10000.00	800.1
308.15	15000.00	803.8
308.15	20000.00	807.5
308.15	25000.00	811.1
308.15	30000.00	814.5
308.15	35000.00	817.8
308.15	40000.00	821.0
308.15	45000.00	824.1
308.15	50000.00	827.1
308.15	55000.00	830.0
308.15	60000.00	832.7
318.15	100.00	783.4
318.15	1000.00	784.2
318.15	5000.00	787.9
318.15	10000.00	792.2
318.15	15000.00	796.3
318.15	20000.00	800.2
318.15	25000.00	803.9
318.15	30000.00	807.5
318.15	35000.00	810.9
318.15	40000.00	814.2
318.15	45000.00	817.5
318.15	50000.00	820.5
318.15	55000.00	823.6
318.15	60000.00	825.8
328.15	100.00	775.0
328.15	1000.00	775.9
328.15	5000.00	779.7
328.15	10000.00	784.2
328.15	15000.00	788.5
328.15	20000.00	792.6
328.15	25000.00	796.5
328.15	30000.00	800.2
328.15	35000.00	803.8
328.15	40000.00	807.2
328.15	45000.00	810.6
328.15	50000.00	813.8
328.15	55000.00	816.9
328.15	60000.00	819.8
338.15	100.00	766.3
338.15	1000.00	767.2
338.15	5000.00	771.3
338.15	10000.00	776.1
338.15	15000.00	780.6
338.15	20000.00	784.9
338.15	25000.00	789.0
338.15	30000.00	792.9
338.15	35000.00	796.6
338.15	40000.00	800.2
338.15	45000.00	803.7
338.15	50000.00	807.0
338.15	55000.00	810.3
338.15	60000.00	813.4
348.15	100.00	757.2
348.15	1000.00	758.3
348.15	5000.00	762.6
348.15	10000.00	767.7
348.15	15000.00	772.5
348.15	20000.00	777.0
348.15	25000.00	781.3
348.15	30000.00	785.4
348.15	35000.00	789.3
348.15	40000.00	793.0
348.15	45000.00	796.6
348.15	50000.00	800.1
348.15	55000.00	803.5
348.15	60000.00	806.5
358.15	100.00	747.7
358.15	1000.00	748.8
358.15	5000.00	753.5
358.15	10000.00	758.8
358.15	15000.00	764.0
358.15	20000.00	768.7
358.15	25000.00	773.3
358.15	30000.00	777.5
358.15	35000.00	781.6
358.15	40000.00	785.5
358.15	45000.00	789.3
358.15	50000.00	792.9
358.15	55000.00	796.4
358.15	60000.00	799.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.20	1000.00	796.7
303.20	2000.00	797.5
303.20	3000.00	798.3
303.20	4000.00	799.2
303.20	5000.00	799.9
303.20	6000.00	800.7
303.20	7000.00	801.5
303.20	8000.00	802.3
303.20	9000.00	803.1
303.20	10000.00	803.9
323.20	1000.00	779.0
323.20	2000.00	779.9
323.20	3000.00	780.8
323.20	4000.00	781.7
323.20	5000.00	782.6
323.20	6000.00	783.5
323.20	7000.00	784.4
323.20	8000.00	785.3
323.20	9000.00	786.2
323.20	10000.00	787.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	803.85
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	799.66
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	807.62
288.15	5000.00	811.32
288.15	10000.00	814.7
288.15	15000.00	817.95
288.15	20000.00	821.27
288.15	25000.00	824.24
288.15	30000.00	827.24
288.15	35000.00	830.04
288.15	40000.00	832.73
293.15	100.00	803.57
293.15	5000.00	807.24
293.15	10000.00	810.8
293.15	15000.00	814.22
293.15	20000.00	817.46
293.15	25000.00	820.74
293.15	30000.00	823.7
293.15	35000.00	826.5
293.15	40000.00	829.09
298.15	100.00	799.61
298.15	5000.00	803.49
298.15	10000.00	807.15
298.15	15000.00	810.5
298.15	20000.00	813.78
298.15	25000.00	816.92
298.15	30000.00	820.04
298.15	35000.00	822.87
298.15	40000.00	825.81
303.15	100.00	795.62
303.15	5000.00	799.57
303.15	10000.00	803.13
303.15	15000.00	806.69
303.15	20000.00	810.14
303.15	25000.00	813.48
303.15	30000.00	816.64
303.15	35000.00	819.75
303.15	40000.00	822.6
308.15	100.00	791.31
308.15	5000.00	795.4
308.15	10000.00	799.21
308.15	15000.00	802.79
308.15	20000.00	806.37
308.15	25000.00	809.72
308.15	30000.00	813.03
308.15	35000.00	816.12
308.15	40000.00	819.06
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	799.54
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	803.17
293.15	5000.00	807.25
293.15	10000.00	811.02
293.15	15000.00	814.54
293.15	20000.00	817.87
293.15	25000.00	821.05
293.15	30000.00	824.15
293.15	35000.00	827.21
303.15	100.00	795.52
303.15	5000.00	799.83
303.15	10000.00	803.8
303.15	15000.00	807.49
303.15	20000.00	810.95
303.15	25000.00	814.23
303.15	30000.00	817.38
303.15	35000.00	820.48
313.15	100.00	787.3
313.15	5000.00	791.61
313.15	10000.00	795.67
313.15	15000.00	799.52
313.15	20000.00	803.19
313.15	25000.00	806.72
313.15	30000.00	810.15
313.15	35000.00	813.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.15	100.00	795.6
303.15	5000.00	799.5
303.15	10000.00	803.4
303.15	15000.00	807.0
303.15	20000.00	810.5
303.15	25000.00	813.9
303.15	30000.00	817.2
313.15	100.00	787.6
313.15	5000.00	791.6
313.15	10000.00	795.7
313.15	15000.00	799.5
313.15	20000.00	803.2
313.15	25000.00	806.7
313.15	30000.00	810.1
323.15	100.00	779.1
323.15	5000.00	783.4
323.15	10000.00	787.7
323.15	15000.00	791.7
323.15	20000.00	795.6
323.15	25000.00	799.3
323.15	30000.00	802.9
333.15	100.00	770.6
333.15	5000.00	775.1
333.15	10000.00	779.6
333.15	15000.00	783.9
333.15	20000.00	787.9
333.15	25000.00	791.8
333.15	30000.00	795.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	810.9
283.15	5000.00	814.7
283.15	10000.00	818.1
283.15	15000.00	821.7
283.15	20000.00	824.9
298.15	100.00	799.0
298.15	5000.00	803.0
298.15	10000.00	806.9
298.15	15000.00	810.6
298.15	20000.00	814.1
313.15	100.00	786.8
313.15	5000.00	791.2
313.15	10000.00	795.3
313.15	15000.00	799.3
313.15	20000.00	803.1
328.15	100.00	774.5
328.15	5000.00	779.1
328.15	10000.00	783.7
328.15	15000.00	787.8
328.15	20000.00	791.9
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
253.15	102.00	1368.034
253.15	5133.00	1393.016
253.15	10109.00	1416.633
253.15	15198.00	1439.865
253.15	20092.00	1461.442
253.15	25341.00	1483.73
253.15	30423.00	1504.606
273.15	101.00	1293.525
273.15	5181.00	1320.802
273.15	10163.00	1346.251
273.15	15287.00	1371.412
273.15	20261.00	1394.803
273.15	25076.00	1416.612
273.15	30164.00	1438.924
293.15	105.00	1222.539
293.15	5042.00	1251.176
293.15	10141.00	1279.332
293.15	15272.00	1306.262
293.15	20136.00	1330.72
293.15	25068.00	1354.567
293.15	30231.00	1378.484
313.15	108.00	1154.108
313.15	5139.00	1185.752
313.15	10136.00	1215.403
313.15	15128.00	1243.591
313.15	20151.00	1270.557
313.15	25136.00	1296.129
313.01	30237.00	1321.177
333.15	101.00	1086.768
333.15	5018.00	1120.458
333.15	10050.00	1152.816
333.15	15186.00	1183.885
333.15	20183.00	1212.543
333.15	25121.00	1239.487
333.15	30028.00	1265.042
353.15	104.00	1018.903
353.15	5034.00	1055.962
353.15	10009.00	1090.768
353.15	15132.00	1124.22
353.15	20099.00	1154.783
353.15	25054.00	1183.626
353.15	30493.00	1213.605
Reference

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
249.99	100.00	1382.6
218.20	102.00	1512.0
299.97	138.00	1199.6
249.99	177.00	1383.0
350.05	270.00	1030.8
400.05	307.00	847.6
218.26	875.00	1515.2
400.05	947.00	854.9
350.07	997.00	1036.3
450.12	1081.00	636.4
249.99	1128.00	1387.7
299.96	1174.00	1206.0
350.07	2073.00	1044.4
218.21	2111.00	1520.8
400.05	2155.00	867.0
450.12	2181.00	653.9
250.01	2296.00	1393.4
299.96	2560.00	1214.3
500.31	4798.00	438.4
400.03	4879.00	893.3
218.26	5018.00	1533.1
299.98	5042.00	1228.8
450.11	5172.00	697.0
350.07	5244.00	1067.5
249.97	5362.00	1408.3
249.94	9322.00	1427.1
218.32	9465.00	1551.0
299.98	9515.00	1254.1
500.32	9558.00	542.3
350.06	9697.00	1098.3
400.07	9768.00	936.6
450.11	9782.00	754.2
218.35	19810.00	1591.6
299.96	19849.00	1308.7
500.32	19968.00	690.2
400.07	19974.00	1015.3
350.08	20259.00	1164.3
450.10	20385.00	860.0
249.90	20903.00	1478.7
400.06	27823.00	1068.3
218.34	29071.00	1626.6
450.11	30113.00	938.6
399.98	30784.00	1087.2
500.31	30851.00	799.1
299.96	39521.00	1400.6
249.93	39564.00	1553.9
500.28	39800.00	870.0
450.13	40189.00	1008.7
399.96	40232.00	1142.9
350.04	40537.00	1273.0
218.31	49499.00	1698.1
299.96	49960.00	1444.6
450.13	50091.00	1069.5
399.98	50284.00	1196.8
500.30	50346.00	946.6
350.03	52186.00	1327.6
249.94	59448.00	1625.8
399.97	59616.00	1242.9
500.31	60509.00	1009.7
350.04	60588.00	1364.3
218.32	61345.00	1736.4
500.31	77533.00	1102.4
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	293.19	1222.98
100.00	298.12	1205.93
100.00	303.12	1188.72
100.00	308.20	1171.37
100.00	313.17	1154.51
100.00	318.20	1137.48
15200.00	293.12	1308.47
15200.00	298.11	1292.86
15200.00	303.14	1277.31
15200.00	308.20	1263.59
15200.00	313.16	1248.7
30400.00	293.22	1379.93
30400.00	298.15	1365.6
30400.00	303.24	1350.89
30400.00	308.13	1336.85
30400.00	313.16	1322.58
30400.00	318.16	1308.73
45590.00	293.21	1444.18
45590.00	298.14	1430.65
45590.00	303.13	1417.04
45590.00	308.13	1403.65
45590.00	313.16	1390.41
45590.00	318.14	1377.4
60790.00	293.21	1502.84
60790.00	298.14	1490.03
60790.00	303.20	1477.02
60790.00	308.13	1464.46
60790.00	313.17	1451.85
60790.00	318.12	1439.64
75990.00	293.20	1557.22
75990.00	298.14	1544.87
75990.00	303.15	1532.53
75990.00	308.12	1520.4
75990.00	313.16	1508.49
75990.00	318.12	1496.85
91190.00	293.20	1607.57
91190.00	298.14	1595.85
91190.00	303.17	1584.03
91190.00	308.20	1572.36
91190.00	313.15	1561.08
91190.00	318.12	1549.89
101320.00	293.18	1639.47
101320.00	298.14	1628.0
101320.00	303.17	1616.49
101320.00	308.19	1605.09
101320.00	313.15	1594.14
101320.00	318.11	1583.33
111450.00	293.17	1669.92
111450.00	298.14	1658.78
111450.00	303.19	1647.55
111450.00	308.16	1636.69
111450.00	313.22	1625.76
111450.00	318.17	1615.27
121580.00	293.16	1699.12
121580.00	298.14	1688.24
121580.00	303.18	1677.36
121580.00	308.11	1666.98
121580.00	313.17	1656.22
121580.00	318.17	1645.95
Reference

Molar volume, m3/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar volume, m3/mol - Liquid
298.15	100.00	0.0001
298.15	10000.00	0.0001
313.15	100.00	0.0001
313.15	10000.00	0.0001
328.15	100.00	0.0001
328.15	10000.00	0.0001
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 5193.51]	kPa	[284.20; 536.78]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.58913e+01
Coefficient B			-3.49716e+03
Coefficient C			-6.00740e+01
Temperature range, min.			284.20
Temperature range, max.			536.78
Pvap	1.33	kPa	284.20	Calculated Property
Pvap	7.57	kPa	312.26	Calculated Property
Pvap	30.35	kPa	340.33	Calculated Property
Pvap	94.50	kPa	368.39	Calculated Property
Pvap	243.45	kPa	396.46	Calculated Property
Pvap	542.12	kPa	424.52	Calculated Property
Pvap	1076.63	kPa	452.59	Calculated Property
Pvap	1951.03	kPa	480.65	Calculated Property
Pvap	3282.18	kPa	508.72	Calculated Property
Pvap	5193.51	kPa	536.78	Calculated Property
Pvap	[6.41e-10; 4954.75]	kPa	[146.95; 536.71]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.17170e+01
Coefficient B			-8.00269e+03
Coefficient C			-7.70223e+00
Coefficient D			3.95045e-07
Temperature range, min.			146.95
Temperature range, max.			536.71
Pvap	6.41e-10	kPa	146.95	Calculated Property
Pvap	2.13e-05	kPa	190.26	Calculated Property
Pvap	0.01	kPa	233.56	Calculated Property
Pvap	0.62	kPa	276.87	Calculated Property
Pvap	10.27	kPa	320.18	Calculated Property
Pvap	76.88	kPa	363.48	Calculated Property
Pvap	341.14	kPa	406.79	Calculated Property
Pvap	1054.26	kPa	450.10	Calculated Property
Pvap	2514.29	kPa	493.40	Calculated Property
Pvap	4954.75	kPa	536.71	Calculated Property

Similar Compounds

Find more compounds similar to 1-Propanol.

Mixtures

• 1-Propanol + Isopropyl Alcohol
• Aniline + 1-Propanol
• 1-Propanol + Acetonitrile
• Benzene + 1-Propanol
• 1-Propanol + Toluene
• Benzene + 1-Propanol + 2-Pyrrolidinone
• 1-Propanol + Toluene + 2-Pyrrolidinone
• 1-Propanol + Acetic acid, methyl ester
• Benzene + 1-Propanol + Cyclohexane
• 1-Propanol + 1-Propanamine, N-propyl-
• 1-Propanol + Piperazine, 1-methyl-
• 1-Propanol + Tetrahydrofuran
• 1-Propanol + Diisopropyl ether
• Benzene + 1-Propanol + Diisopropyl ether
• 1,3-Dioxolane + 1-Propanol + Water
• 1-Propanol + Phenol, 2-methyl-
• 1-Propanol + p-Cresol
• 1-Propanol + 2-Butanone + Benzene, 1,3-dichloro-
• 1-Propanol + Di-n-propyl ether
• 1-Propanol + 1-Pentanol

Find more mixtures with 1-Propanol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
• Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
• Application of the Extended Langmuir Model for the Determination of Lyophobicity of 1-Propanol in Acetonitrile
• Topological Investigations of Excess Molar Volumes and Excess Isentropic Compressibilities of Ternary Mixtures Containing Pyrrolidin-2-one at 308.15 K
• Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
• Solubility of Baicalein in Different Solvents from (287 to 323) K
• Fluid Phase Topology of Benzene + Cyclohexane + 1-Propanol at 101.3 kPa
• Isobaric vapor-liquid equilibria for 1-propanol +water + copper(II) chloride at 100 kPa
• Solubility of thiopene in carbon dioxide and carbon dioxide + 1-propanol mixtures at temperatures from 313 to 363K
• Thermodynamics of mixtures with strongly negative deviations from Raoult s law Part 9. Vapor liquid equilibria for the system 1-propanol + di-n-propylamine at six temperatures between 293.15 and 318.15K
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
• Prediction and experimental verification of the effect of salt on the vapour liquid equilibrium of ethanol/1-propanol/water mixture
• Thermodynamic properties of mixtures containing ionic liquids Vapor pressures and activity coefficients of n-alcohols and benzene in binary mixtures with 1-methyl-3-butyl-imidazolium bis(trifluoromethyl-sulfonyl) imide
• Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
• Salt effect on vapor liquid equilibria for binary systems of propanol/CaCl2 and butanol/CaCl2
• Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
• Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15K
• (Liquid + liquid) equilibria of (water + 1-propanol + solvent) at T = 298.2K
• Effect of anion fluorination in 1-ethyl-3-methylimidazolium as solvent for the liquid extraction of ethanol from ethyl tert-butyl ether
• Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
• Volumetric and derivative properties under pressure for the system 1-propanol + toluene: A discussion of PC-SAFT and SAFT-VR
• Isobaric vapor-liquid equilibria for the binary systems 1-propyl alcohol + dipropyl ether and 1-butyl alcohol + dibutyl ether at 20 and 101.3 kPa
• Vapor liquid equilibria in the ternary system dipropyl ether + 1-propanol + 1-pentanol and the binary systems dipropyl ether + 1-pentanol, 1-propanol + 1-pentanol at 101.3 kPa
• Vapor liquid equilibria for the ternary mixture of carbon dioxide + 1-propanol + propyl acetate at elevated pressures
• Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2K
• Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using 2-ethoxyethanol as entrainer
• Vapor liquid equilibrium, densities, and interfacial tensions for the system ethyl 1,1-dimethylethyl ether (ETBE) + propan-1-ol
• High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
• Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
• Liquid liquid equilibria for the ternary systems water + 1-propanol + methyl methacrylate, +butyl methacrylate, and +isobutyl methacrylate
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
• Isothermal vapor liquid equilibrium at 303.15K and excess molar volumes at 298.15 K for the ternary system of propyl vinyl ether + 1-propanol + 2,2,4-trimethyl-pentane and its binary sub-systems
• Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
• Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
• Apparent molar volume, isentropic compressibility and conductivity of di-sodium hydrogen phosphate in water and in aqueous solutions of 1-propanol
• Liquid liquid equilibria of the systems dipropyl ether + n-propanol +water and dipropyl ether + n-propanol + ethylene glycol at different temperatures
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
• Volumetric, isentropic compressibility and electrical conductivity of solutions of tri-sodium phosphate in 1-propanol +water mixed-solvent media over the temperature range of 283.15 303.15K
• Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Experimental densities and derived thermodynamic properties of liquid propan-1-ol at temperatures from 298 to 423K and at pressures up to 40MPa
• Excess molar enthalpies of ethyl acetoacetate + (methanol, +ethanol, +1-propanol, and +2-propanol) at T = (298.15, 313.15 and 328.15)K and p = (0.1 and 10.0)MPa
• Liquid liquid equilibria for the binary system of di-isopropyl ether (DIPE) +water in between 288.15 and 323.15K and the ternary systems of DIPE +water + C1 C4 alcohols at 298.15K
• A new high-pressure vapour liquid equilibrium apparatus
• Solubility of l-serine, l-threonine and l-isoleucine in aqueous aliphatic alcohol solutions
• Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
• Study of the effect of increasing the chain length of the alkane in excess molar enthalpies of mixtures containing methyl tert-butyl ether, 1-propanol, alkane
• Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes at 298.15K for the ternary system di-isopropyl ether + n-propyl alcohol + toluene and its binary subsystems
• Isothermal vapor liquid equilibrium at 323.15K and excess molar volumes and refractive indices at 298.15K for the ternary system propyl vinyl ether + 1-propanol + benzene and its binary sub-systems
• Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
• Solubility of antioxidant 1010 in pure alkanols
• Measurement and prediction of tie-line data for mixtures of (water + 1-propanol + diisopropyl ether): LLE diagrams as a function of temperature
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• Solubility of CF4 in lower alcohols
• Liquid-liquid equilibrium of (water + 1-propanol + 1-pentanol) system at 298.15 and 323.15 K
• New analytic apparatus for experimental determination of vapor-liquid equilibria and saturation densities
• Isothermal vapour liquid equilibria in the binary and ternary systems consisting of an ionic liquid, 1-propanol and CO2
• Isobaric vapor-liquid equilibria for water + n-propanol + n-butanol ternary system at atmospheric pressure
• Solubilities of cefodizime disodium in aqueous alcohol mixtures at atmospheric pressure and different temperatures
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Solubility of alpha-form and beta-form of L-glutamic acid in different aqueous solvent mixtures
• Phase equilibria on binary systems containing diethyl sulfide
• Solubility of HFCs in lower alcohols
• VLE of CO2 + glycerol + (ethanol or 1-propanol or 1-butanol)
• Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol
• Vapor-liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography
• P-x data for binary systems using a novel static total pressure apparatus
• Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
• Determination of the crystallization thermodynamics and kinetics of L-tryptophan in alcohols - water system
• Study of the influence of the structure of the alcohol on vapor pressures and osmotic coefficients of binary mixtures alcohol + 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at T = 323.15 K
• Study of the liquid-liquid equilibrium of 1-propanol + manganese sulphate and 2-propanol + lithium sulphate aqueous two-phase systems at different temperatures: Experiment and correlation
• Solubility of caprolactam in different organic solvents
• Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
• Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
• Thermodynamic study of aqueous two phase systems for some aliphatic alcohols + sodium thiosulfate + water
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Solid-liquid phase equilibrium of glyphosate in selected solvents
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Liquid liquid equilibrium of 1-propanol, 2-propanol, 2-methyl-2-propanol or 2-butanol + sodium sulfite + water aqueous two phase systems
• Vapour-liquid and chemical equilibria in the ethyl ethanoate + ethanol + propyl ethanoate + propanol system accompanied with transesterification reaction
• Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
• Measurement and correlation for solubility of levofloxacin in six solvents at temperatures from 288.15 to 328.15 K
• Solubility of lansoprazole in different solvents
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
• Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
• The study of phase behavior of aqueous 1-propanol/2-propanol/2-butanol/2-methyl-2-propanol systems in the presence of disodium tartrate or disodium succinate at T = 298.15 K
• Solid liquid equilibrium of 1-hydroxyethane-1,1-diphosphonic acid in different solvents
• Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
• Solubility of dimethyl fumarate in water + (methanol, ethanol, 1-propanol) from (278.15 to 333.15) K
• Correlation of solubility of pioglitazone hydrochloride in different binary solvents
• Solubility of citric acid in water, ethanol, n-propanol and in mixtures of ethanol + water
• The effect of temperature on the liquid-liquid equilibria of somealiphatic alcohols + di-sodium hydrogen citrate + water systems: Experimental and correlation
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
• Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
• Biobutanol and n-propanol recovery using a low density phosphonium based ionic liquid at T = 298.15 K and p = 1 atm
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
• Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
• Liquid liquid equilibria of 4-methyl-2-pentanone + 1-propanol or 2-propanol + water ternary systems: Measurements and correlation at different temperatures
• (p, VE, T) Measurements of mixtures (DBE + alcohol) at temperaturesfrom (293.15 to 353.15) K and at pressures up to 140 MPa
• Liquid-liquid equilibria of 1-octyl-3-methylimidazolium hexafluorophosphate with 1-propanol or tert-butanol in the critical region
• Thermodynamics of fenofibrate and solubility in pure organic solvents
• Present status of the modified UNIFAC Model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solubility, liquid-liquid equilibrium and critical states for the system acetic acid + n-propanol + n-propyl acetate + water at 293.15 K and 303.15 K
• Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
• Micellization properties and related thermodynamic parameters ofaqueous sodium dodecyl sulfate and sodium dodecyl sulfonatesolutions in the presence of 1-propanol
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
• Excess molar enthalpies for binary mixtures of n-propanol, acetic acid, and n-propyl acetate at 313.15 K and atmospheric pressure
• Solid-liquid equilibrium of sulbactam in pure solvents and binary solvent mixtures
• Experimental study of the density and derived partial molar volumes of complex ternary water+1-propanol+Li2SO4 mixtures at temperatures from (303 to 448) K and pressures up to 40 MPa
• Measurement, correlation, and prediction of vapor pressure for binary and ternary systems containing an ionic liquid 1,3-dimethylimidazolium methylsulfate
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Isobaric vapor liquid equilibrium for the binary systems of 1-propanol + 1-(methoxymethoxy)-butane and 1-butanol + 1-(methoxymethoxy)- butane at 101.3 kPa
• Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
• Correlation of solubility and calculation of thermodynamic properties of guanidine nitrate in different solvents
• Solubility of methylphosphonic acid in selected organic solvents
• Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
• Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Measurement, correlation, and prediction of vapor pressure for binary and ternary systems containing an alkylsulfate-based ionic liquid
• Liquid-liquid equilibria for water + 1-propanol (or 1-butanol) + potassium chloride + ammonium chloride quaternary systems at 298.15 K
• High-temperature vapor-liquid equilibrium for ethanol-1-propanol mixtures and modeling with SAFT-VR
• Measurements and correlations of density and viscosity for short chain (C1-C3) n-alcohol - water mixtures in the temperature range from 350.7 K to 476.2 K at pressures up to 40 MPa
• Isobaric (vapor-liquid) equilibria for binary systems of methanol + 1-(methoxymethoxy)- propane and 1-propanol + 1-(methoxymethoxy)-propane at 101.33 kPa
• Excess molar enthalpies of the ternary mixture n-propanol + acetic acid + water at 313.15 K and atmospheric pressure
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• The liquid-liquid phase separation and crystallization of vanillin in 1-propanol/water solution
• Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• Liquid-liquid equilibrium for the quaternary system propionic acid + n-propanol + n-propyl propionate + water at 293.15, 313.15 and 333.15 K
• Measurement and correlation of phase equilibria for ternary systems of water + (ethanol / 1-propanol) + 1-decyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide at 298.15 K
• Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
• Measurement and correlation of liquid-liquid equilibria at different temperatures of water + 1-propanol + 1-ethyl-3- methylimidazolium bis(trifluoromethylsulfonyl)imide or 1-hexyl-3- methylimidazolium bis(trifluoromethylsulfonyl)imide ternary systems
• Determination and correlation of solubility of linezolid form II in different pure and binary solvents
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• Application of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate to the removal of alcohol from mixtures with heptane
• Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
• Heterogeneous azeotropic distillation for the separation of n-propanol + water mixture using n-propyl acetate as entrainer
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Measurement and correlation of density and viscosity of n-alcohol-water mixtures at temperatures up to 618 K and at pressures up to 40 MPa
• Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• SLLE and SLLVE of the water + NH4Cl + 1-propanol system at 101.3 kPa
• Measurement and correlation of aqueous biphasic systems composed of alcohol (1-propanol/ 2-propanol/tert-butanol) + (NH4)2SO4 + H2O at 298 K and a textile dye partition.
• Capability study of 1-butyl-3- methylimidazolium bis(trifluoromethylsulfonyl)imide and trihexyl(tetradecyl)phosphonium bis(2,4,4-trimethylpentyl)phosphinate as solvents in the separation of 1-propanol from water
• Molecular dynamic simulation, molecular interactions and structural properties of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide + 1-butanol/1- propanol mixtures at (298.15-323.15) K and 0.1 M Pa
• Solubility evaluation and thermodynamic modeling of beta-lapachone in water and ten organic solvents at different temperatures
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
• Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
• (Vapor + liquid) equilibria for the binary mixtures (1-propanol + dibromomethane, or + bromochloromethane, or + 1,2-dichloroethane or +1-bromo-2-chloroethane) at T = 313.15 K.
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Excess molar enthalpies of ethylformate and (1-propanol, 2-propanol, 1-butanol, 2-butanol, and 1-pentanol) at T = (298.15 and 308.15) K and p = (5 and 10) MPa
• Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
• Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
• Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
• Volumetric properties of binary mixtures of ionic liquid 1-butyl-3-methylimidazolium octylsulfate with water or propanol in the temperature range of 278.15 K to 328.15 K
• Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Densities, viscosities, and ultrasonic velocity studies of binary mixtures of trichloromethane with methanol, ethanol, propan-1-ol, and butan-1-ol at T=(298.15 and 308.15) K
• Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
• Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
• Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
• Densities and volumetric properties of (formamide + ethanol, or 1-propanol, or 1,2-ethanediol, or 1,2-propanediol) mixtures at temperatures between 293.15 K and 318.15 K
• Molar excess enthalpies of binary mixtures of [tributyl phosphate + {CH3(CH2)nOH (n = 0 to 3)}] at 298.15 K
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
• Isobaric (vapour + liquid + liquid) equilibrium data for (di-n-propyl ether + n-propyl alcohol + water) and (diisopropyl ether + isopropyl alcohol + water) systems at 100 kPa
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
• Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
• Thermodynamic properties of solutions of sodium di-hydrogen phosphate in (1-propanol + water) mixed-solvent media over the temperature range of (283.15 to 303.15) K
• Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
• Excess molar volumes and isentropic compressibility of binary systems {trioctylmethylammonium bis(trifluoromethysulfonyl)imide + methanol or ethanol or 1-propanol} at different temperatures
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Osmotic coefficients of binary mixtures of 1-butyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate with alcohols at T = 323.15 K
• Phase equilibria study of the binary systems (N-butyl-4-methylpyridinium tosylate ionic liquid + an alcohol)
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Density and viscosity of 1-butyl-3-methylimidazolium nitrate with ethanol, 1-propanol, or 1-butanol at several temperatures
• Vapour pressures and osmotic coefficients of binary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate and 1-ethyl-3-methylpyridinium ethylsulfate with alcohols at T = 323.15 K
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
• Measurement and modeling of high-pressure (vapour + liquid) equilibria of (CO2 + alcohol) binary systems
• Vapour pressures, osmotic and activity coefficients for binary mixtures containing (1-ethylpyridinium ethylsulfate + several alcohols) at T = 323.15 K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Isobaric (vapour + liquid) equilibria for the (1-propanol + 1-butanol) binary mixture at (53.3 and 91.3) kPa
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
• Measurement and correlation of solubilities of apigenin and apigenin 7-O-rhamnosylglucoside in seven solvents at different temperatures
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Thermophysical properties of {(+-)-linalool + propan-1-ol}: A first stage towards the development of a green process
• Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Apparent molar volumes and compressibilities of tetrabutyl-ammonium bromide in organic solvents
• Measurement and modeling of osmotic coefficients of binary mixtures (alcohol + 1,3-dimethylpyridinium methylsulfate) at T = 323.15 K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Determination and modelling of osmotic coefficients and vapour pressures of binary systems 1- and 2-propanol with CnMimNTf2 ionic liquids (n = 2, 3, and 4) at T = 323.15 K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Application of the extended real associated solution (ERAS) theory to excess molar enthalpies of benzaldehyde + 1-alkanols (C1 to C5) at T = 298.15 K
• Phase equilibrium in systems with ionic liquids: An example for the downstream process of the Biphasic Acid Scavenging utilizing Ionic Liquids (BASIL) process. Part I: Experimental data
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1 C4) and dimethyl carbonate
• Solubility of sodium 4-nitrotoluene-2-sulfonate in (propanol + water) and (ethylene glycol + water) systems
• Effect of the temperature on the physical properties of pure 1-propyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide an