Chemical Properties of Octane (CAS 111-65-9)

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InChI

InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3

InChI Key

TVMXDCGIABBOFY-UHFFFAOYSA-N

Formula

C8H18

SMILES

CCCCCCCC

Molecular Weight¹

114.23

CAS

111-65-9

Other Names

• Oktan
• Oktanen
• Ottani
• UN 1262
• n-C8H18
• n-Octane

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• 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_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• 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_subH : Enthalpy of sublimation 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).
• ν : Kinematic viscosity (m²/s).
• 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.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• 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).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• 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	0.3980		KDB
Tig	493.15	K	KDB
AP	343.750	K	KDB
ΔcH°liquid	[-5471.80; -5270.40]	kJ/mol
ΔcH°liquid	-5470.30 ± 1.60	kJ/mol	NIST
ΔcH°liquid	-5470.71 ± 0.67	kJ/mol	NIST
ΔcH°liquid	-5466.60	kJ/mol	NIST
ΔcH°liquid	-5471.80 ± 5.40	kJ/mol	NIST
ΔcH°liquid	-5441.30	kJ/mol	NIST
ΔcH°liquid	Outlier -5270.40	kJ/mol	NIST
μ	0.00	debye	KDB
η	[0.0005180; 0.0005180]	Pa×s
η	0.0005180	Pa×s	Study o...
η	0.0005180	Pa×s	Study o...
η	0.0005180	Pa×s	Thermop...
LFL	1.00	% in Air	KDB
UFL	6.50	% in Air	KDB
Tflash,oc	286.48	K	KDB
ΔfG°	16.40	kJ/mol	KDB
Rg	4.6800		KDB
Δc,grossH	5470.71	kJ/mol	KDB
Δc,netH	5074.565	kJ/mol	KDB
ΔfH°gas	[-208.70; -208.40]	kJ/mol
ΔfH°gas	-208.60	kJ/mol	KDB
ΔfH°gas	-208.70	kJ/mol	NIST
ΔfH°gas	-208.40 ± 0.67	kJ/mol	NIST
ΔfH°liquid	[-250.30; -250.00]	kJ/mol
ΔfH°liquid	-250.30 ± 1.80	kJ/mol	NIST
ΔfH°liquid	-250.00 ± 0.84	kJ/mol	NIST
ΔfusH°	16.48	kJ/mol	Joback Calculated Property
ΔvapH°	[34.00; 41.60]	kJ/mol
ΔvapH°	41.53	kJ/mol	NIST
ΔvapH°	41.60	kJ/mol	NIST
ΔvapH°	41.50 ± 0.10	kJ/mol	NIST
ΔvapH°	41.50 ± 0.10	kJ/mol	NIST
ΔvapH°	41.50	kJ/mol	NIST
ΔvapH°	41.60 ± 0.08	kJ/mol	NIST
ΔvapH°	41.60 ± 0.08	kJ/mol	NIST
ΔvapH°	41.50 ± 0.10	kJ/mol	NIST
ΔvapH°	41.48	kJ/mol	NIST
ΔvapH°	Outlier 34.00	kJ/mol	NIST
IE	[9.71; 10.25]	eV
IE	9.80 ± 0.15	eV	NIST
IE	10.01	eV	NIST
IE	9.80 ± 0.10	eV	NIST
IE	9.71 ± 0.15	eV	NIST
IE	9.79	eV	NIST
IE	10.25	eV	NIST
log10WS	[-5.24; -5.24]
log10WS	-5.24		Aq. Sol...
log10WS	-5.24		Estimat...
logPoct/wat	3.367		Crippen Calculated Property
McVol	123.580	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[2470.00; 2497.12]	kPa
Pc	2490.00	kPa	KDB
Pc	2496.00	kPa	Measure...
Pc	2496.00	kPa	Experim...
Pc	2496.00	kPa	Measure...
Pc	2496.00	kPa	Determi...
Pc	2490.00 ± 30.00	kPa	NIST
Pc	2495.00 ± 20.00	kPa	NIST
Pc	2487.00	kPa	NIST
Pc	2480.00 ± 5.00	kPa	NIST
Pc	2490.00 ± 30.00	kPa	NIST
Pc	2486.93 ± 17.23	kPa	NIST
Pc	2486.20 ± 40.53	kPa	NIST
Pc	2488.00 ± 40.53	kPa	NIST
Pc	2492.59 ± 50.66	kPa	NIST
Pc	2497.10 ± 20.00	kPa	NIST
Pc	2497.12 ± 19.99	kPa	NIST
Pc	Outlier 2470.00 ± 98.07	kPa	NIST
S°gas	467.06 ± 0.92	J/mol×K	NIST
S°liquid	[359.80; 361.20]	J/mol×K
S°liquid	361.20	J/mol×K	NIST
S°liquid	359.80	J/mol×K	NIST
S°liquid	359.80	J/mol×K	NIST
Tboil	[393.15; 401.65]	K
Tboil	398.82	K	KDB
Tboil	398.57	K	Isobari...
Tboil	398.83	K	Solutio...
Tboil	398.83	K	Solutio...
Tboil	398.79	K	Isother...
Tboil	398.60	K	Excess ...
Tboil	399.15	K	Excess ...
Tboil	398.79	K	Vapor-L...
Tboil	398.65	K	Densiti...
Tboil	398.83	K	Measure...
Tboil	398.80	K	Isobari...
Tboil	398.85	K	Multipr...
Tboil	398.49	K	Measure...
Tboil	398.74	K	Measure...
Tboil	398.96	K	Isobari...
Tboil	398.80 ± 0.20	K	NIST
Tboil	398.80 ± 0.20	K	NIST
Tboil	398.90	K	NIST
Tboil	398.73 ± 0.10	K	NIST
Tboil	398.80	K	NIST
Tboil	398.76 ± 0.20	K	NIST
Tboil	398.96 ± 0.20	K	NIST
Tboil	398.96 ± 0.50	K	NIST
Tboil	398.93 ± 0.08	K	NIST
Tboil	398.70 ± 0.50	K	NIST
Tboil	398.75 ± 0.15	K	NIST
Tboil	398.55 ± 0.20	K	NIST
Tboil	398.12 ± 0.20	K	NIST
Tboil	398.77 ± 0.10	K	NIST
Tboil	398.95 ± 0.40	K	NIST
Tboil	398.76 ± 0.20	K	NIST
Tboil	398.75 ± 0.50	K	NIST
Tboil	398.55 ± 0.30	K	NIST
Tboil	398.77 ± 0.15	K	NIST
Tboil	398.27 ± 0.30	K	NIST
Tboil	399.00 ± 0.60	K	NIST
Tboil	398.40 ± 1.00	K	NIST
Tboil	398.85 ± 0.25	K	NIST
Tboil	398.82 ± 0.30	K	NIST
Tboil	399.15 ± 1.50	K	NIST
Tboil	397.80 ± 0.30	K	NIST
Tboil	Outlier 396.40 ± 2.00	K	NIST
Tboil	398.85 ± 0.40	K	NIST
Tboil	399.09 ± 0.30	K	NIST
Tboil	398.75 ± 0.10	K	NIST
Tboil	398.81 ± 0.44	K	NIST
Tboil	398.55 ± 0.30	K	NIST
Tboil	398.71 ± 0.20	K	NIST
Tboil	398.80 ± 0.40	K	NIST
Tboil	398.95 ± 0.50	K	NIST
Tboil	Outlier 393.15 ± 3.00	K	NIST
Tboil	398.81 ± 0.10	K	NIST
Tboil	398.90 ± 0.20	K	NIST
Tboil	398.25 ± 0.30	K	NIST
Tboil	398.62 ± 0.30	K	NIST
Tboil	397.85 ± 0.30	K	NIST
Tboil	397.20 ± 2.00	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.80 ± 0.40	K	NIST
Tboil	398.85 ± 0.50	K	NIST
Tboil	397.35 ± 0.50	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.90 ± 0.30	K	NIST
Tboil	398.75 ± 0.40	K	NIST
Tboil	398.81 ± 0.01	K	NIST
Tboil	397.65 ± 0.50	K	NIST
Tboil	397.40 ± 1.00	K	NIST
Tboil	398.15 ± 2.00	K	NIST
Tboil	398.70 ± 0.20	K	NIST
Tboil	398.95 ± 0.50	K	NIST
Tboil	398.90 ± 0.20	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.81 ± 0.10	K	NIST
Tboil	398.80 ± 0.30	K	NIST
Tboil	397.15 ± 1.00	K	NIST
Tboil	398.75 ± 0.20	K	NIST
Tboil	Outlier 401.65 ± 0.50	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.90 ± 0.20	K	NIST
Tboil	398.81 ± 0.20	K	NIST
Tboil	398.95 ± 0.20	K	NIST
Tboil	398.80 ± 0.05	K	NIST
Tboil	398.55 ± 0.50	K	NIST
Tboil	398.15 ± 0.60	K	NIST
Tboil	Outlier 396.00 ± 2.00	K	NIST
Tboil	398.55 ± 0.50	K	NIST
Tboil	398.75 ± 0.50	K	NIST
Tboil	398.74 ± 0.10	K	NIST
Tboil	398.35 ± 0.30	K	NIST
Tboil	398.55 ± 0.50	K	NIST
Tboil	398.74 ± 0.15	K	NIST
Tboil	397.75 ± 0.50	K	NIST
Tboil	398.95 ± 0.20	K	NIST
Tboil	398.15 ± 1.00	K	NIST
Tboil	397.65 ± 0.30	K	NIST
Tboil	399.00 ± 0.70	K	NIST
Tboil	399.00 ± 1.00	K	NIST
Tboil	398.15 ± 1.00	K	NIST
Tboil	398.95 ± 0.30	K	NIST
Tboil	398.15 ± 2.00	K	NIST
Tboil	398.95 ± 0.30	K	NIST
Tboil	398.64 ± 0.10	K	NIST
Tboil	398.45 ± 0.50	K	NIST
Tboil	Outlier 396.70 ± 1.50	K	NIST
Tc	[568.70; 568.92]	K
Tc	568.70	K	KDB
Tc	568.90	K	Measure...
Tc	568.92	K	Experim...
Tc	568.80	K	The Cri...
Tc	568.90	K	Measure...
Tc	568.92	K	Determi...
Tfus	[216.26; 216.30]	K
Tfus	216.26	K	Aq. Sol...
Tfus	216.30	K	KDB
Ttriple	[215.60; 216.37]	K
Ttriple	216.37	K	KDB
Ttriple	216.37 ± 0.40	K	NIST
Ttriple	216.37 ± 0.03	K	NIST
Ttriple	216.36 ± 0.20	K	NIST
Ttriple	216.37 ± 0.20	K	NIST
Ttriple	216.36 ± 0.05	K	NIST
Ttriple	216.37 ± 0.02	K	NIST
Ttriple	215.80 ± 0.20	K	NIST
Ttriple	215.85 ± 0.20	K	NIST
Ttriple	Outlier 215.60 ± 0.25	K	NIST
Vc	[0.492; 0.492]	m3/kmol
Vc	0.492	m3/kmol	KDB
Vc	0.492	m3/kmol	NIST
Zc	0.2590860		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[232.74; 297.00]	J/mol×K	[385.65; 523.15]
Cp,gas	232.74 ± 0.47	J/mol×K	385.65	NIST
Cp,gas	238.95 ± 0.48	J/mol×K	398.15	NIST
Cp,gas	242.67	J/mol×K	405.70	NIST
Cp,gas	250.59 ± 0.50	J/mol×K	423.15	NIST
Cp,gas	263.02 ± 0.53	J/mol×K	448.15	NIST
Cp,gas	270.70	J/mol×K	462.50	NIST
Cp,gas	274.84 ± 0.55	J/mol×K	473.15	NIST
Cp,gas	285.98 ± 0.57	J/mol×K	498.15	NIST
Cp,gas	295.39	J/mol×K	522.70	NIST
Cp,gas	297.00 ± 0.59	J/mol×K	523.15	NIST
Cp,liquid	[247.70; 269.31]	J/mol×K	[283.15; 333.15]
Cp,liquid	248.16	J/mol×K	283.15	Excess ...
Cp,liquid	248.20	J/mol×K	283.15	Measure...
Cp,liquid	250.10	J/mol×K	288.15	Excess ...
Cp,liquid	250.10	J/mol×K	288.15	Measure...
Cp,liquid	250.12	J/mol×K	288.15	Thermod...
Cp,liquid	252.06	J/mol×K	293.15	Measure...
Cp,liquid	252.24	J/mol×K	293.15	Excess ...
Cp,liquid	247.70	J/mol×K	293.70	NIST
Cp,liquid	252.40	J/mol×K	297.54	NIST
Cp,liquid	252.40	J/mol×K	298.00	NIST
Cp,liquid	253.20	J/mol×K	298.00	NIST
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	254.18	J/mol×K	298.15	NIST
Cp,liquid	254.08	J/mol×K	298.15	Measure...
Cp,liquid	253.98	J/mol×K	298.15	Excess ...
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	253.89	J/mol×K	298.15	NIST
Cp,liquid	254.11	J/mol×K	298.15	NIST
Cp,liquid	254.14	J/mol×K	298.15	NIST
Cp,liquid	253.94	J/mol×K	298.15	Thermod...
Cp,liquid	253.72	J/mol×K	298.15	NIST
Cp,liquid	254.07	J/mol×K	298.15	NIST
Cp,liquid	252.92	J/mol×K	298.15	NIST
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	254.02	J/mol×K	298.15	NIST
Cp,liquid	251.50	J/mol×K	298.30	NIST
Cp,liquid	254.70	J/mol×K	299.00	NIST
Cp,liquid	253.93	J/mol×K	299.80	NIST
Cp,liquid	256.16	J/mol×K	303.15	Measure...
Cp,liquid	256.50	J/mol×K	303.16	Excess ...
Cp,liquid	258.28	J/mol×K	308.15	Measure...
Cp,liquid	258.03	J/mol×K	308.15	Thermod...
Cp,liquid	258.05	J/mol×K	308.15	Excess ...
Cp,liquid	260.45	J/mol×K	313.15	Measure...
Cp,liquid	260.87	J/mol×K	313.16	Excess ...
Cp,liquid	262.66	J/mol×K	318.15	Measure...
Cp,liquid	262.70	J/mol×K	318.15	Excess ...
Cp,liquid	262.20	J/mol×K	318.15	NIST
Cp,liquid	264.78	J/mol×K	323.15	Excess ...
Cp,liquid	267.24	J/mol×K	328.15	Excess ...
Cp,liquid	269.31	J/mol×K	333.15	Excess ...
η	[0.0000323; 0.0007180]	Pa×s	[273.15; 583.10]
η	0.0007180	Pa×s	273.15	Densiti...
η	0.0006710	Pa×s	278.15	Densiti...
η	0.0006130	Pa×s	283.15	Density...
η	0.0006247	Pa×s	283.15	Liquid ...
η	0.0006230	Pa×s	283.15	Densiti...
η	0.0006140	Pa×s	283.15	A Study...
η	0.0005850	Pa×s	288.15	Densiti...
η	0.0005840	Pa×s	288.15	Densiti...
η	0.0005433	Pa×s	293.15	Densiti...
η	0.0005340	Pa×s	293.15	Densiti...
η	0.0005560	Pa×s	293.15	Densiti...
η	0.0005380	Pa×s	293.15	Dynamic...
η	0.0005410	Pa×s	293.15	Density...
η	0.0005450	Pa×s	293.15	Volumet...
η	0.0005420	Pa×s	293.15	A Study...
η	0.0005470	Pa×s	293.15	Excess ...
η	0.0005374	Pa×s	293.15	Viscosi...
η	0.0005460	Pa×s	293.15	Excess ...
η	0.0005464	Pa×s	293.15	Physica...
η	0.0005450	Pa×s	293.15	Viscosi...
η	0.0005380	Pa×s	293.15	Dynamic...
η	0.0005520	Pa×s	293.15	Densiti...
η	0.0005450	Pa×s	293.15	Densiti...
η	0.0005439	Pa×s	293.15	Densiti...
η	0.0005523	Pa×s	293.15	Liquid ...
η	0.0005060	Pa×s	298.15	Dynamic...
η	0.0005170	Pa×s	298.15	Excess ...
η	0.0005087	Pa×s	298.15	Viscosi...
η	0.0005100	Pa×s	298.15	Density...
η	0.0005060	Pa×s	298.15	Dynamic...
η	0.0005230	Pa×s	298.15	Densiti...
η	0.0005177	Pa×s	298.15	Densiti...
η	0.0005206	Pa×s	298.15	Thermod...
η	0.0005123	Pa×s	298.15	Physica...
η	0.0005210	Pa×s	298.15	Excess ...
η	0.0005140	Pa×s	298.15	Excess ...
η	0.0005080	Pa×s	298.15	A Study...
η	0.0005108	Pa×s	298.15	Densiti...
η	0.0005010	Pa×s	298.15	Densiti...
η	0.0005130	Pa×s	298.15	Viscosi...
η	0.0005140	Pa×s	298.15	Densiti...
η	0.0005290	Pa×s	298.15	Densiti...
η	0.0005130	Pa×s	298.15	Volumet...
η	0.0004780	Pa×s	303.15	Dynamic...
η	0.0004860	Pa×s	303.15	Densiti...
η	0.0004840	Pa×s	303.15	Viscosi...
η	0.0004830	Pa×s	303.15	Physica...
η	0.0004720	Pa×s	303.15	Densiti...
η	0.0004900	Pa×s	303.15	Excess ...
η	0.0004830	Pa×s	303.15	A Study...
η	0.0005010	Pa×s	303.15	Densiti...
η	0.0004837	Pa×s	303.15	Thermod...
η	0.0004820	Pa×s	303.15	Excess ...
η	0.0004810	Pa×s	303.15	Density...
η	0.0004960	Pa×s	303.15	Densiti...
η	0.0004910	Pa×s	303.15	Excess ...
η	0.0004828	Pa×s	303.15	Liquid ...
η	0.0004910	Pa×s	303.15	Density...
η	0.0004780	Pa×s	303.15	Dynamic...
η	0.0004795	Pa×s	303.15	Densiti...
η	0.0004850	Pa×s	303.15	Volumet...
η	0.0004948	Pa×s	303.20	Viscosi...
η	0.0004911	Pa×s	303.20	Viscosi...
η	0.0005014	Pa×s	303.20	Experim...
η	0.0004913	Pa×s	303.20	Viscosi...
η	0.0004590	Pa×s	308.15	Volumet...
η	0.0004560	Pa×s	308.15	Excess ...
η	0.0004590	Pa×s	308.15	Densiti...
η	0.0004500	Pa×s	308.15	Density...
η	0.0004670	Pa×s	308.15	Excess ...
η	0.0004680	Pa×s	308.15	Excess ...
η	0.0004730	Pa×s	308.15	Densiti...
η	0.0004420	Pa×s	313.15	Excess ...
η	0.0004358	Pa×s	313.15	Densiti...
η	0.0004320	Pa×s	313.15	Liquid ...
η	0.0004306	Pa×s	313.15	Thermod...
η	0.0004500	Pa×s	313.15	Densiti...
η	0.0004340	Pa×s	313.15	Densiti...
η	0.0004330	Pa×s	313.15	Volumet...
η	0.0004150	Pa×s	313.15	Density...
η	0.0004560	Pa×s	313.15	Densiti...
η	0.0004220	Pa×s	313.15	Densiti...
η	0.0004340	Pa×s	313.15	Viscosi...
η	0.0004470	Pa×s	313.15	Excess ...
η	0.0004300	Pa×s	313.15	A Study...
η	0.0004431	Pa×s	313.30	Viscosi...
η	0.0004426	Pa×s	313.30	Viscosi...
η	0.0004414	Pa×s	313.30	Viscosi...
η	0.0004150	Pa×s	318.15	Densiti...
η	0.0004310	Pa×s	318.15	Densiti...
η	0.0004120	Pa×s	318.15	Volumet...
η	0.0003800	Pa×s	323.15	Densiti...
η	0.0004120	Pa×s	323.15	Densiti...
η	0.0003940	Pa×s	323.15	Densiti...
η	0.0003864	Pa×s	323.15	Thermod...
η	0.0003870	Pa×s	323.15	Liquid ...
η	0.0003920	Pa×s	323.15	Volumet...
η	0.0003961	Pa×s	323.20	Viscosi...
η	0.0003967	Pa×s	323.20	Viscosi...
η	0.0003979	Pa×s	323.20	Viscosi...
η	0.0003950	Pa×s	328.15	Densiti...
η	0.0003750	Pa×s	328.15	Densiti...
η	0.0003790	Pa×s	333.15	Densiti...
η	0.0003570	Pa×s	333.15	Densiti...
η	0.0003430	Pa×s	333.15	Densiti...
η	0.0003495	Pa×s	333.15	Thermod...
η	0.0003617	Pa×s	333.20	Viscosi...
η	0.0003632	Pa×s	333.20	Viscosi...
η	0.0003634	Pa×s	333.20	Viscosi...
η	0.0003650	Pa×s	338.15	Densiti...
η	0.0003520	Pa×s	343.15	Densiti...
η	0.0003140	Pa×s	343.15	Densiti...
η	0.0003139	Pa×s	343.15	Thermod...
η	0.0003311	Pa×s	343.20	Viscosi...
η	0.0003308	Pa×s	343.20	Viscosi...
η	0.0003352	Pa×s	343.20	Viscosi...
η	0.0003079	Pa×s	348.15	Liquid ...
η	0.0003078	Pa×s	353.10	Experim...
η	0.0003012	Pa×s	353.10	Viscosi...
η	0.0003032	Pa×s	353.10	Viscosi...
η	0.0003013	Pa×s	353.10	Viscosi...
η	0.0002840	Pa×s	353.15	Thermod...
η	0.0002870	Pa×s	353.15	Densiti...
η	0.0002610	Pa×s	363.15	Densiti...
η	0.0002775	Pa×s	363.20	Viscosi...
η	0.0002766	Pa×s	363.20	Viscosi...
η	0.0002765	Pa×s	363.20	Viscosi...
η	0.0002487	Pa×s	373.15	Liquid ...
η	0.0002545	Pa×s	373.30	Viscosi...
η	0.0002540	Pa×s	373.30	Viscosi...
η	0.0002580	Pa×s	373.30	Viscosi...
η	0.0002379	Pa×s	383.00	Viscosi...
η	0.0002341	Pa×s	383.00	Viscosi...
η	0.0002340	Pa×s	383.00	Viscosi...
η	0.0002202	Pa×s	393.10	Viscosi...
η	0.0002208	Pa×s	393.10	Viscosi...
η	0.0002205	Pa×s	393.10	Viscosi...
η	0.0002028	Pa×s	398.15	Liquid ...
η	0.0002019	Pa×s	403.20	Viscosi...
η	0.0002070	Pa×s	403.20	Experim...
η	0.0002040	Pa×s	403.20	Viscosi...
η	0.0002021	Pa×s	403.20	Viscosi...
η	0.0001924	Pa×s	413.20	Viscosi...
η	0.0001902	Pa×s	413.20	Viscosi...
η	0.0001905	Pa×s	413.20	Viscosi...
η	0.0001665	Pa×s	423.15	Liquid ...
η	0.0001775	Pa×s	423.20	Viscosi...
η	0.0001761	Pa×s	423.20	Viscosi...
η	0.0001762	Pa×s	423.20	Viscosi...
η	0.0001643	Pa×s	433.10	Viscosi...
η	0.0001642	Pa×s	433.10	Viscosi...
η	0.0001642	Pa×s	433.10	Viscosi...
η	0.0001514	Pa×s	443.20	Viscosi...
η	0.0001526	Pa×s	443.20	Viscosi...
η	0.0001527	Pa×s	443.20	Viscosi...
η	0.0001393	Pa×s	448.15	Liquid ...
η	0.0001428	Pa×s	453.10	Viscosi...
η	0.0001416	Pa×s	453.10	Viscosi...
η	0.0001465	Pa×s	453.10	Experim...
η	0.0001417	Pa×s	453.10	Viscosi...
η	0.0001321	Pa×s	463.20	Viscosi...
η	0.0001318	Pa×s	463.20	Viscosi...
η	0.0001322	Pa×s	463.20	Viscosi...
η	0.0001241	Pa×s	473.10	Viscosi...
η	0.0001228	Pa×s	473.10	Viscosi...
η	0.0001228	Pa×s	473.10	Viscosi...
η	0.0001168	Pa×s	473.15	Liquid ...
η	0.0001152	Pa×s	483.10	Viscosi...
η	0.0001138	Pa×s	483.10	Viscosi...
η	0.0001139	Pa×s	483.10	Viscosi...
η	0.0001068	Pa×s	493.10	Viscosi...
η	0.0001072	Pa×s	493.10	Viscosi...
η	0.0001069	Pa×s	493.10	Viscosi...
η	0.0000947	Pa×s	498.15	Liquid ...
η	0.0000993	Pa×s	503.00	Viscosi...
η	0.0000995	Pa×s	503.00	Viscosi...
η	0.0001049	Pa×s	503.00	Experim...
η	0.0000983	Pa×s	503.00	Viscosi...
η	0.0000901	Pa×s	513.20	Viscosi...
η	0.0000904	Pa×s	513.20	Viscosi...
η	0.0000755	Pa×s	523.15	Liquid ...
η	0.0000826	Pa×s	523.30	Viscosi...
η	0.0000825	Pa×s	523.30	Viscosi...
η	0.0000753	Pa×s	533.40	Viscosi...
η	0.0000751	Pa×s	533.40	Viscosi...
η	0.0000678	Pa×s	543.40	Viscosi...
η	0.0000678	Pa×s	543.40	Viscosi...
η	0.0000607	Pa×s	553.40	Viscosi...
η	0.0000609	Pa×s	553.40	Viscosi...
η	0.0000692	Pa×s	553.40	Experim...
η	0.0000532	Pa×s	563.30	Viscosi...
η	0.0000534	Pa×s	563.30	Viscosi...
η	0.0000446	Pa×s	573.30	Viscosi...
η	0.0000444	Pa×s	573.30	Viscosi...
η	0.0000323	Pa×s	583.10	Viscosi...
η	0.0000325	Pa×s	583.10	Viscosi...
ΔfusH	[20.09; 21.80]	kJ/mol	[215.60; 216.60]
ΔfusH	20.09	kJ/mol	215.60	NIST
ΔfusH	20.65	kJ/mol	215.80	NIST
ΔfusH	20.74	kJ/mol	216.38	NIST
ΔfusH	20.74	kJ/mol	216.40	NIST
ΔfusH	21.80	kJ/mol	216.60	NIST
ΔsubH	68.10	kJ/mol	216.00	NIST
ΔvapH	[34.41; 44.40]	kJ/mol	[247.00; 537.50]
ΔvapH	44.40	kJ/mol	247.00	NIST
ΔvapH	43.00	kJ/mol	257.00	NIST
ΔvapH	41.75	kJ/mol	298.00	Enthalp...
ΔvapH	38.00 ± 0.10	kJ/mol	311.00	NIST
ΔvapH	40.50 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	41.90	kJ/mol	315.50	NIST
ΔvapH	36.70 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	39.10 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	35.40 ± 0.10	kJ/mol	344.00	NIST
ΔvapH	41.20	kJ/mol	348.50	NIST
ΔvapH	41.00	kJ/mol	348.50	NIST
ΔvapH	37.80 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	39.20	kJ/mol	363.00	NIST
ΔvapH	34.41	kJ/mol	398.80	NIST
ΔvapH	34.41	kJ/mol	398.80	KDB
ΔvapH	36.30	kJ/mol	414.00	NIST
ΔvapH	39.40	kJ/mol	443.00	NIST
ΔvapH	35.50	kJ/mol	469.00	NIST
ΔvapH	34.90	kJ/mol	537.50	NIST
ν	[0.0000007; 0.0000008]	m2/s	[293.15; 298.15]
ν	0.0000008	m2/s	293.15	Densiti...
ν	0.0000007	m2/s	298.15	Densiti...
Pvap	[10.59; 199.97]	kPa	[333.15; 425.20]
Pvap	10.59	kPa	333.15	An equi...
Pvap	16.04	kPa	343.15	An equi...
Pvap	19.31	kPa	348.15	Vapor-L...
Pvap	21.09	kPa	350.64	Measure...
Pvap	23.14	kPa	353.05	Measure...
Pvap	23.61	kPa	353.15	An equi...
Pvap	23.16	kPa	353.15	Measure...
Pvap	25.56	kPa	355.76	Measure...
Pvap	26.66	kPa	356.74	Vapor-L...
Pvap	26.70	kPa	356.97	Measure...
Pvap	28.55	kPa	358.82	Measure...
Pvap	30.00	kPa	359.76	Measure...
Pvap	30.00	kPa	360.06	Measure...
Pvap	31.58	kPa	361.59	Measure...
Pvap	33.52	kPa	363.15	Vapor-L...
Pvap	33.91	kPa	363.15	An equi...
Pvap	34.16	kPa	363.86	Measure...
Pvap	36.53	kPa	365.82	Measure...
Pvap	38.88	kPa	367.65	Measure...
Pvap	40.00	kPa	367.97	Vapor L...
Pvap	40.00	kPa	368.30	Vapor L...
Pvap	40.00	kPa	368.32	Vapor L...
Pvap	40.82	kPa	369.09	Measure...
Pvap	43.19	kPa	370.77	Measure...
Pvap	45.57	kPa	372.39	Measure...
Pvap	48.04	kPa	374.01	Measure...
Pvap	50.59	kPa	375.61	Measure...
Pvap	53.33	kPa	376.95	Vapor-L...
Pvap	52.90	kPa	377.00	Measure...
Pvap	55.02	kPa	378.25	Measure...
Pvap	58.20	kPa	380.03	Measure...
Pvap	60.00	kPa	380.43	Measure...
Pvap	60.00	kPa	380.76	Vapor L...
Pvap	60.00	kPa	380.78	Vapor L...
Pvap	60.00	kPa	380.82	Vapor L...
Pvap	60.00	kPa	380.84	Vapor L...
Pvap	60.00	kPa	380.85	Vapor L...
Pvap	60.00	kPa	380.87	Vapor L...
Pvap	60.00	kPa	380.94	Vapor L...
Pvap	60.00	kPa	380.94	Measure...
Pvap	60.63	kPa	381.34	Measure...
Pvap	62.68	kPa	382.42	Measure...
Pvap	64.25	kPa	383.15	Vapor-L...
Pvap	64.09	kPa	383.15	Ternary...
Pvap	65.07	kPa	383.64	Measure...
Pvap	67.34	kPa	384.76	Measure...
Pvap	70.52	kPa	386.29	Measure...
Pvap	73.02	kPa	387.45	Measure...
Pvap	75.43	kPa	388.55	Measure...
Pvap	77.94	kPa	389.65	Measure...
Pvap	80.05	kPa	390.56	Measure...
Pvap	95.10	kPa	391.15	(Vapor ...
Pvap	82.51	kPa	391.60	Measure...
Pvap	84.94	kPa	392.60	Measure...
Pvap	87.09	kPa	393.47	Measure...
Pvap	90.00	kPa	394.09	Measure...
Pvap	89.39	kPa	394.37	Measure...
Pvap	90.00	kPa	394.60	Measure...
Pvap	91.38	kPa	395.14	Measure...
Pvap	93.64	kPa	396.04	Measure...
Pvap	96.14	kPa	396.95	Measure...
Pvap	98.73	kPa	397.90	Measure...
Pvap	99.59	kPa	398.19	Measure...
Pvap	101.30	kPa	398.49	Measure...
Pvap	101.33	kPa	398.57	Isobari...
Pvap	100.68	kPa	398.59	Measure...
Pvap	101.30	kPa	398.74	Measure...
Pvap	101.30	kPa	398.79	Vapor-L...
Pvap	101.30	kPa	398.80	Isobari...
Pvap	101.32	kPa	398.83	Solutio...
Pvap	101.32	kPa	398.83	Measure...
Pvap	101.32	kPa	398.85	Multipr...
Pvap	101.33	kPa	398.96	Isobari...
Pvap	103.61	kPa	399.61	Measure...
Pvap	106.23	kPa	400.53	Measure...
Pvap	108.30	kPa	401.23	Measure...
Pvap	110.71	kPa	402.03	Measure...
Pvap	113.09	kPa	402.81	Measure...
Pvap	114.65	kPa	403.32	Measure...
Pvap	116.17	kPa	403.81	Measure...
Pvap	117.10	kPa	404.10	Measure...
Pvap	119.25	kPa	404.79	Measure...
Pvap	121.60	kPa	405.51	Measure...
Pvap	124.10	kPa	406.27	Measure...
Pvap	126.61	kPa	407.03	Measure...
Pvap	129.50	kPa	407.89	Measure...
Pvap	132.46	kPa	408.75	Measure...
Pvap	135.53	kPa	409.62	Measure...
Pvap	137.42	kPa	410.15	Measure...
Pvap	139.87	kPa	410.83	Measure...
Pvap	185.56	kPa	422.10	Measure...
Pvap	188.02	kPa	422.64	Measure...
Pvap	190.85	kPa	423.26	Measure...
Pvap	193.15	kPa	423.76	Measure...
Pvap	195.02	kPa	424.15	Measure...
Pvap	197.87	kPa	424.76	Measure...
Pvap	199.97	kPa	425.20	Measure...
n0	[1.38550; 1.53910]		[277.80; 318.15]
n0	1.40400		277.80	The mea...
n0	1.40320		279.68	The mea...
n0	1.40280		280.36	The mea...
n0	1.40270		280.51	The mea...
n0	1.40210		281.66	The mea...
n0	1.40170		282.65	The mea...
n0	1.40120		283.88	The mea...
n0	1.40070		284.73	The mea...
n0	1.39980		288.15	Thermod...
n0	1.39750		293.15	Infinit...
n0	1.39730		293.15	Thermod...
n0	1.39760		293.15	DIELECT...
n0	1.39650		293.15	Isobari...
n0	1.39730		293.15	Vapor-L...
n0	1.39690		293.15	Excess ...
n0	1.39730		293.15	Isother...
n0	1.39780		293.15	Experim...
n0	1.39910		293.15	DIELECT...
n0	1.39700		293.15	Densiti...
n0	1.39730		293.15	Limitin...
n0	1.39600		293.15	Experim...
n0	1.39780		293.15	Isother...
n0	1.39650		293.15	Physica...
n0	1.39640		293.23	The liq...
n0	1.39590		294.23	The liq...
n0	1.39540		295.29	The liq...
n0	1.39490		296.27	The liq...
n0	1.39440		297.41	The liq...
n0	1.39780		298.10	Excess ...
n0	1.39519		298.15	Extract...
n0	1.39500		298.15	Excess ...
n0	1.39519		298.15	Extract...
n0	1.39519		298.15	Liquid-...
n0	1.39519		298.15	(Liquid...
n0	1.39500		298.15	(P,Vm,T...
n0	1.39480		298.15	Excess ...
n0	1.39519		298.15	Separat...
n0	1.39500		298.15	p, Vm, ...
n0	1.39520		298.15	Multipr...
n0	1.39470		298.15	Excess ...
n0	1.39500		298.15	Excess ...
n0	1.39490		298.15	Thermod...
n0	1.39460		298.15	Liquid-...
n0	1.39470		298.15	Physica...
n0	1.39510		298.15	Fully a...
n0	1.39550		298.15	Measure...
n0	1.39670		298.15	DIELECT...
n0	1.39460		298.15	Activit...
n0	1.39510		298.15	Isobari...
n0	1.39520		298.15	DIELECT...
n0	1.39540		298.15	Solubil...
n0	1.39480		298.15	The den...
n0	1.39538		298.15	Liquid ...
n0	1.39460		298.15	Vapor l...
n0	1.39520		298.15	A Study...
n0	1.39504		298.15	Separat...
n0	1.39800		298.15	P-rho-T...
n0	1.53910		298.15	(Vapor ...
n0	1.39530		298.15	Isother...
n0	1.39510		298.15	Density...
n0	1.39460		298.15	Ternary...
n0	1.39505		298.15	KDB
n0	1.39390		298.48	The liq...
n0	1.39340		299.50	The liq...
n0	1.39290		303.15	DIELECT...
n0	1.39230		303.15	Densiti...
n0	1.39240		303.15	Thermod...
n0	1.39260		303.15	Physica...
n0	1.39260		303.15	Excess ...
n0	1.39160		303.15	Excess ...
n0	1.39450		303.15	DIELECT...
n0	1.39040		308.15	Excess ...
n0	1.38880		308.15	Excess ...
n0	1.39040		308.15	The den...
n0	1.38770		313.15	Excess ...
n0	1.38550		318.15	Multipr...
n0	1.38680		318.15	The den...
ρl	[643.83; 718.58]	kg/m3	[273.15; 363.15]
ρl	718.58	kg/m3	273.15	Densiti...
ρl	718.25	kg/m3	273.15	Experim...
ρl	714.31	kg/m3	278.15	Experim...
ρl	714.61	kg/m3	278.15	Densiti...
ρl	710.61	kg/m3	283.15	Density...
ρl	710.34	kg/m3	283.15	Experim...
ρl	710.62	kg/m3	283.15	Densiti...
ρl	710.76	kg/m3	283.15	Measure...
ρl	706.35	kg/m3	288.15	Experim...
ρl	706.62	kg/m3	288.15	Densiti...
ρl	706.76	kg/m3	288.15	Measure...
ρl	706.81	kg/m3	288.15	DIELECT...
ρl	706.58	kg/m3	288.15	Excess ...
ρl	706.54	kg/m3	288.15	Thermod...
ρl	706.99	kg/m3	288.15	Thermod...
ρl	706.54	kg/m3	288.15	Densiti...
ρl	706.60	kg/m3	288.15	Study o...
ρl	706.58	kg/m3	288.15	Analysi...
ρl	704.13	kg/m3	291.15	Measure...
ρl	704.17	kg/m3	291.15	Solutio...
ρl	704.10	kg/m3	291.15	Multipr...
ρl	703.00	kg/m3	293.00	KDB
ρl	702.60	kg/m3	293.15	Dynamic...
ρl	702.82	kg/m3	293.15	Excess ...
ρl	702.44	kg/m3	293.15	Isother...
ρl	702.61	kg/m3	293.15	Physica...
ρl	702.57	kg/m3	293.15	Analysi...
ρl	702.57	kg/m3	293.15	Excess ...
ρl	702.74	kg/m3	293.15	Measure...
ρl	702.53	kg/m3	293.15	Densiti...
ρl	702.57	kg/m3	293.15	Dynamic...
ρl	705.60	kg/m3	293.15	Viscosi...
ρl	702.54	kg/m3	293.15	Volumet...
ρl	702.50	kg/m3	293.15	Densiti...
ρl	702.50	kg/m3	293.15	Densiti...
ρl	703.00	kg/m3	293.15	Thermod...
ρl	702.55	kg/m3	293.15	Density...
ρl	702.87	kg/m3	293.15	Excess ...
ρl	702.64	kg/m3	293.15	Liquid ...
ρl	702.60	kg/m3	293.15	Infinit...
ρl	708.00	kg/m3	293.15	Isobari...
ρl	703.00	kg/m3	293.15	Experim...
ρl	702.77	kg/m3	293.15	DIELECT...
ρl	702.61	kg/m3	293.15	Densiti...
ρl	702.44	kg/m3	293.15	Vapor-L...
ρl	702.50	kg/m3	293.15	Densiti...
ρl	702.76	kg/m3	293.15	Densiti...
ρl	702.76	kg/m3	293.15	Limitin...
ρl	702.60	kg/m3	293.15	Density...
ρl	702.53	kg/m3	293.15	Thermod...
ρl	702.86	kg/m3	293.15	Excess ...
ρl	702.54	kg/m3	293.15	A Study...
ρl	702.93	kg/m3	293.15	Surface...
ρl	702.50	kg/m3	293.15	Densiti...
ρl	702.35	kg/m3	293.15	Experim...
ρl	703.88	kg/m3	293.15	Densiti...
ρl	702.69	kg/m3	293.20	Isother...
ρl	700.59	kg/m3	295.20	Isother...
ρl	698.98	kg/m3	297.20	Isother...
ρl	706.60	kg/m3	298.10	Excess ...
ρl	698.51	kg/m3	298.10	Excess ...
ρl	698.86	kg/m3	298.15	Determi...
ρl	698.81	kg/m3	298.15	Excess ...
ρl	698.60	kg/m3	298.15	Multipr...
ρl	698.73	kg/m3	298.15	Excess ...
ρl	698.58	kg/m3	298.15	Study o...
ρl	698.73	kg/m3	298.15	Densiti...
ρl	698.60	kg/m3	298.15	(Liquid...
ρl	698.55	kg/m3	298.15	Density...
ρl	698.49	kg/m3	298.15	Volumet...
ρl	698.92	kg/m3	298.15	Thermod...
ρl	698.60	kg/m3	298.15	Evaluat...
ρl	698.40	kg/m3	298.15	Fully a...
ρl	698.75	kg/m3	298.15	Thermod...
ρl	698.84	kg/m3	298.15	Liquid-...
ρl	698.60	kg/m3	298.15	Extract...
ρl	698.85	kg/m3	298.15	Excess ...
ρl	698.50	kg/m3	298.15	Thermod...
ρl	698.76	kg/m3	298.15	Thermod...
ρl	697.36	kg/m3	298.15	Excess ...
ρl	698.34	kg/m3	298.15	Experim...
ρl	698.58	kg/m3	298.15	Study o...
ρl	698.57	kg/m3	298.15	Densiti...
ρl	698.73	kg/m3	298.15	DIELECT...
ρl	698.64	kg/m3	298.15	Thermod...
ρl	698.62	kg/m3	298.15	Excess ...
ρl	698.60	kg/m3	298.15	The den...
ρl	698.63	kg/m3	298.15	Excess ...
ρl	698.61	kg/m3	298.15	Excess ...
ρl	698.60	kg/m3	298.15	Excess ...
ρl	698.53	kg/m3	298.15	Density...
ρl	698.58	kg/m3	298.15	Study o...
ρl	698.60	kg/m3	298.15	Extract...
ρl	698.60	kg/m3	298.15	Measure...
ρl	698.55	kg/m3	298.15	Analysi...
ρl	698.49	kg/m3	298.15	Liquid-...
ρl	698.50	kg/m3	298.15	Densiti...
ρl	698.60	kg/m3	298.15	Excess ...
ρl	698.59	kg/m3	298.15	Excess ...
ρl	698.60	kg/m3	298.15	Liquid-...
ρl	698.60	kg/m3	298.15	Separat...
ρl	698.71	kg/m3	298.15	Measure...
ρl	698.57	kg/m3	298.15	Physica...
ρl	698.55	kg/m3	298.15	Excess ...
ρl	698.60	kg/m3	298.15	Thermop...
ρl	698.49	kg/m3	298.15	Ternary...
ρl	698.49	kg/m3	298.15	Liquid-...
ρl	698.64	kg/m3	298.15	Thermod...
ρl	698.50	kg/m3	298.15	Dynamic...
ρl	698.71	kg/m3	298.15	Liquid-...
ρl	698.86	kg/m3	298.15	Applica...
ρl	698.86	kg/m3	298.15	Study o...
ρl	698.52	kg/m3	298.15	Solutio...
ρl	698.49	kg/m3	298.15	Activit...
ρl	698.55	kg/m3	298.15	Thermod...
ρl	698.45	kg/m3	298.15	Measure...
ρl	698.70	kg/m3	298.15	Liquid-...
ρl	698.50	kg/m3	298.15	Viscosi...
ρl	701.60	kg/m3	298.15	Viscosi...
ρl	698.61	kg/m3	298.15	Isobari...
ρl	698.64	kg/m3	298.15	Liquid ...
ρl	698.72	kg/m3	298.15	Excess ...
ρl	698.49	kg/m3	298.15	Vapor l...
ρl	698.50	kg/m3	298.15	Densiti...
ρl	699.90	kg/m3	298.15	Thermod...
ρl	699.83	kg/m3	298.15	Densiti...
ρl	698.60	kg/m3	298.15	(Vapor ...
ρl	698.72	kg/m3	298.15	Excess ...
ρl	698.64	kg/m3	298.15	Thermod...
ρl	698.50	kg/m3	298.15	Densiti...
ρl	698.50	kg/m3	298.15	Densiti...
ρl	698.54	kg/m3	298.15	Dynamic...
ρl	698.50	kg/m3	298.15	Density...
ρl	698.50	kg/m3	298.15	Solubil...
ρl	698.51	kg/m3	298.15	Densiti...
ρl	698.57	kg/m3	298.20	Apparen...
ρl	698.26	kg/m3	298.20	Isother...
ρl	698.68	kg/m3	298.20	Isobari...
ρl	697.13	kg/m3	299.50	Isother...
ρl	694.50	kg/m3	303.15	Study o...
ρl	694.88	kg/m3	303.15	Thermod...
ρl	695.72	kg/m3	303.15	Thermod...
ρl	693.90	kg/m3	303.15	Density...
ρl	692.56	kg/m3	303.15	Excess ...
ρl	694.70	kg/m3	303.15	DIELECT...
ρl	695.79	kg/m3	303.15	Densiti...
ρl	694.50	kg/m3	303.15	Densiti...
ρl	694.49	kg/m3	303.15	Density...
ρl	694.30	kg/m3	303.15	Experim...
ρl	694.48	kg/m3	303.15	Analysi...
ρl	694.52	kg/m3	303.15	Densiti...
ρl	694.52	kg/m3	303.15	Vapor-L...
ρl	694.80	kg/m3	303.15	Excess ...
ρl	694.69	kg/m3	303.15	Densiti...
ρl	694.49	kg/m3	303.15	Dynamic...
ρl	694.67	kg/m3	303.15	Activit...
ρl	694.48	kg/m3	303.15	Excess ...
ρl	694.50	kg/m3	303.15	Dynamic...
ρl	694.56	kg/m3	303.15	Physica...
ρl	694.60	kg/m3	303.15	Excess ...
ρl	694.75	kg/m3	303.15	Excess ...
ρl	694.50	kg/m3	303.15	Densiti...
ρl	694.35	kg/m3	303.15	A Study...
ρl	694.50	kg/m3	303.15	Density...
ρl	694.66	kg/m3	303.15	Measure...
ρl	694.48	kg/m3	303.15	Densiti...
ρl	694.44	kg/m3	303.15	Volumet...
ρl	694.50	kg/m3	303.15	Study o...
ρl	690.42	kg/m3	308.15	Densiti...
ρl	690.50	kg/m3	308.15	Excess ...
ρl	690.42	kg/m3	308.15	Excess ...
ρl	690.44	kg/m3	308.15	Excess ...
ρl	690.37	kg/m3	308.15	Volumet...
ρl	690.43	kg/m3	308.15	Excess ...
ρl	690.44	kg/m3	308.15	Densiti...
ρl	690.34	kg/m3	308.15	Thermod...
ρl	690.67	kg/m3	308.15	DIELECT...
ρl	690.58	kg/m3	308.15	Measure...
ρl	690.44	kg/m3	308.15	Density...
ρl	690.73	kg/m3	308.15	Excess ...
ρl	690.45	kg/m3	308.15	Excess ...
ρl	690.50	kg/m3	308.15	The den...
ρl	690.42	kg/m3	308.15	Analysi...
ρl	690.31	kg/m3	308.15	Solutio...
ρl	690.72	kg/m3	308.15	Study o...
ρl	690.48	kg/m3	308.15	Study o...
ρl	690.24	kg/m3	308.15	Experim...
ρl	690.42	kg/m3	308.15	Study o...
ρl	690.40	kg/m3	308.15	Density...
ρl	690.68	kg/m3	308.15	Excess ...
ρl	690.42	kg/m3	308.15	Study o...
ρl	686.63	kg/m3	313.15	Excess ...
ρl	686.17	kg/m3	313.15	Experim...
ρl	686.29	kg/m3	313.15	Volumet...
ρl	686.36	kg/m3	313.15	Density...
ρl	686.49	kg/m3	313.15	Measure...
ρl	686.34	kg/m3	313.15	Densiti...
ρl	686.30	kg/m3	313.15	Densiti...
ρl	686.59	kg/m3	313.15	Excess ...
ρl	687.50	kg/m3	313.15	Thermod...
ρl	687.59	kg/m3	313.15	Densiti...
ρl	686.30	kg/m3	313.15	Densiti...
ρl	687.00	kg/m3	313.15	Density...
ρl	686.52	kg/m3	313.15	Densiti...
ρl	686.39	kg/m3	313.15	Liquid ...
ρl	686.12	kg/m3	313.15	A Study...
ρl	686.35	kg/m3	313.15	Densiti...
ρl	686.37	kg/m3	313.20	Apparen...
ρl	682.37	kg/m3	318.15	Measure...
ρl	682.10	kg/m3	318.15	Densiti...
ρl	682.24	kg/m3	318.15	Densiti...
ρl	682.20	kg/m3	318.15	The den...
ρl	682.20	kg/m3	318.15	Multipr...
ρl	682.19	kg/m3	318.15	Volumet...
ρl	682.47	kg/m3	318.15	Excess ...
ρl	682.06	kg/m3	318.15	Solutio...
ρl	682.50	kg/m3	318.15	Study o...
ρl	682.16	kg/m3	318.15	Measure...
ρl	682.49	kg/m3	318.15	Excess ...
ρl	682.06	kg/m3	318.15	Experim...
ρl	682.23	kg/m3	318.15	Densiti...
ρl	682.26	kg/m3	318.15	Density...
ρl	678.09	kg/m3	323.15	Densiti...
ρl	678.11	kg/m3	323.15	Densiti...
ρl	678.08	kg/m3	323.15	Volumet...
ρl	679.37	kg/m3	323.15	Thermod...
ρl	679.34	kg/m3	323.15	Densiti...
ρl	677.94	kg/m3	323.15	Experim...
ρl	678.13	kg/m3	323.15	Density...
ρl	674.54	kg/m3	328.15	Excess ...
ρl	674.56	kg/m3	328.15	Excess ...
ρl	673.92	kg/m3	328.15	Densiti...
ρl	673.95	kg/m3	328.15	Densiti...
ρl	673.79	kg/m3	328.15	Experim...
ρl	674.10	kg/m3	328.15	Multipr...
ρl	674.55	kg/m3	328.15	Excess ...
ρl	674.15	kg/m3	328.15	Measure...
ρl	669.77	kg/m3	333.15	Densiti...
ρl	670.98	kg/m3	333.15	Densiti...
ρl	671.02	kg/m3	333.15	Thermod...
ρl	669.61	kg/m3	333.15	Experim...
ρl	669.71	kg/m3	333.15	Densiti...
ρl	665.51	kg/m3	338.15	Densiti...
ρl	665.40	kg/m3	338.15	Experim...
ρl	665.55	kg/m3	338.15	Densiti...
ρl	661.24	kg/m3	343.15	Densiti...
ρl	661.16	kg/m3	343.15	Experim...
ρl	662.54	kg/m3	343.15	Thermod...
ρl	662.59	kg/m3	343.15	Densiti...
ρl	661.28	kg/m3	343.15	Densiti...
ρl	656.88	kg/m3	348.15	Experim...
ρl	656.96	kg/m3	348.15	Densiti...
ρl	652.63	kg/m3	353.15	Densiti...
ρl	652.57	kg/m3	353.15	Experim...
ρl	653.80	kg/m3	353.15	Thermod...
ρl	654.05	kg/m3	353.15	Densiti...
ρl	648.23	kg/m3	358.15	Experim...
ρl	648.26	kg/m3	358.15	Densiti...
ρl	645.68	kg/m3	363.15	Densiti...
ρl	643.85	kg/m3	363.15	Densiti...
ρl	643.83	kg/m3	363.15	Experim...
ΔfusS	[93.19; 95.85]	J/mol×K	[215.60; 216.38]
ΔfusS	93.19	J/mol×K	215.60	NIST
ΔfusS	95.70	J/mol×K	215.80	NIST
ΔfusS	95.85	J/mol×K	216.38	NIST
csound,fluid	[1112.00; 1214.46]	m/s	[288.15; 313.15]
csound,fluid	1213.60	m/s	288.15	Analysi...
csound,fluid	1213.60	m/s	288.15	Excess ...
csound,fluid	1214.46	m/s	288.15	Thermod...
csound,fluid	1193.00	m/s	293.15	Dynamic...
csound,fluid	1193.32	m/s	293.15	Thermod...
csound,fluid	1193.00	m/s	293.15	Excess ...
csound,fluid	1192.90	m/s	293.15	Analysi...
csound,fluid	1193.00	m/s	293.15	Dynamic...
csound,fluid	1171.90	m/s	298.15	Excess ...
csound,fluid	1172.70	m/s	298.15	Study o...
csound,fluid	1172.70	m/s	298.15	Study o...
csound,fluid	1172.00	m/s	298.15	Excess ...
csound,fluid	1171.90	m/s	298.15	Analysi...
csound,fluid	1172.41	m/s	298.15	Thermod...
csound,fluid	1173.00	m/s	298.15	Dynamic...
csound,fluid	1172.09	m/s	298.15	Thermod...
csound,fluid	1170.88	m/s	298.15	Thermop...
csound,fluid	1173.00	m/s	298.15	Dynamic...
csound,fluid	1170.38	m/s	298.15	Liquid ...
csound,fluid	1152.00	m/s	303.15	Dynamic...
csound,fluid	1152.00	m/s	303.15	Excess ...
csound,fluid	1151.48	m/s	303.15	Thermod...
csound,fluid	1148.00	m/s	303.15	Density...
csound,fluid	1152.10	m/s	303.15	Study o...
csound,fluid	1151.00	m/s	303.15	Excess ...
csound,fluid	1150.90	m/s	303.15	Analysi...
csound,fluid	1152.00	m/s	303.15	Dynamic...
csound,fluid	1152.10	m/s	303.15	Study o...
csound,fluid	1131.70	m/s	308.15	Study o...
csound,fluid	1130.30	m/s	308.15	Excess ...
csound,fluid	1130.30	m/s	308.15	Analysi...
csound,fluid	1131.70	m/s	308.15	Study o...
csound,fluid	1132.00	m/s	308.15	Density...
csound,fluid	1112.00	m/s	313.15	Density...
γ	[0.00; 0.02]	N/m	[283.15; 523.15]
γ	0.02	N/m	283.15	Liquid ...
γ	0.02	N/m	293.15	Liquid ...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Density...
γ	0.02	N/m	298.15	Density...
γ	0.02	N/m	298.15	Interfa...
γ	0.02	N/m	298.15	Analysi...
γ	0.02	N/m	303.15	Density...
γ	0.02	N/m	303.15	Liquid ...
γ	0.02	N/m	308.15	Density...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Interfa...
γ	0.02	N/m	313.15	Density...
γ	0.02	N/m	313.15	Liquid ...
γ	0.02	N/m	318.15	Interfa...
γ	0.02	N/m	323.15	Liquid ...
γ	0.02	N/m	348.15	Liquid ...
γ	0.01	N/m	373.15	Liquid ...
γ	0.01	N/m	398.15	Liquid ...
γ	0.01	N/m	423.15	Liquid ...
γ	0.01	N/m	448.15	Liquid ...
γ	0.01	N/m	473.15	Liquid ...
γ	0.00	N/m	498.15	Liquid ...
γ	0.00	N/m	523.15	Liquid ...
λ	[0.12; 0.13]	W/m×K	[294.50; 334.80]
λ	0.13	W/m×K	294.50	Thermal...
λ	0.12	W/m×K	314.70	Thermal...
λ	0.12	W/m×K	334.80	Thermal...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[352.83; 397.87]	K	[22.95; 99.01]
Tboil	352.83	K	22.95	A novel...
Tboil	360.22	K	29.98	A novel...
Tboil	366.89	K	37.87	A novel...
Tboil	371.89	K	44.82	A novel...
Tboil	376.93	K	52.81	A novel...
Tboil	380.87	K	59.85	A novel...
Tboil	384.36	K	66.66	A novel...
Tboil	388.38	K	75.23	A novel...
Tboil	391.59	K	82.72	A novel...
Tboil	394.32	K	89.51	A novel...
Tboil	397.87	K	99.01	A novel...

Datasets

1. Viscosity, Pa*s of Octane
2. Mass density, kg/m3 of Octane
3. Viscosity, Pa*s of Octane
4. Mass density, kg/m3 of Octane
5. Viscosity, Pa*s of Octane
6. Mass density, kg/m3 of Octane
7. Mass density, kg/m3 of Octane
8. Mass density, kg/m3 of Octane
9. Mass density, kg/m3 of Octane
10. Speed of sound, m/s of Octane
11. Molar heat capacity at constant pressure, J/K/mol of Octane
12. Mass density, kg/m3 of Octane
13. Viscosity, Pa*s of Octane
14. Mass density, kg/m3 of Octane
15. Mass density, kg/m3 of Octane
16. Viscosity, Pa*s of Octane
17. Speed of sound, m/s of Octane
18. Speed of sound, m/s of Octane
19. Mass density, kg/m3 of Octane
20. Thermal conductivity, W/m/K of Octane
21. Viscosity, Pa*s of Octane
22. Mass density, kg/m3 of Octane
23. Relative permittivity at various frequencies of Octane
24. Viscosity, Pa*s of Octane
25. Mass density, kg/m3 of Octane

Viscosity, Pa*s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Viscosity, Pa*s of Octane - Liquid
273.15	100.00	0.0007
273.15	10000.00	0.0008
273.15	20000.00	0.0009
273.15	30000.00	0.0010
293.15	100.00	0.0005
293.15	10000.00	0.0006
293.15	20000.00	0.0007
293.15	30000.00	0.0007
313.15	100.00	0.0004
313.15	10000.00	0.0005
313.15	20000.00	0.0005
313.15	30000.00	0.0006
333.15	100.00	0.0004
333.15	10000.00	0.0004
333.15	20000.00	0.0004
333.15	30000.00	0.0005

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
273.15	100.00	719.0
273.15	10000.00	726.0
273.15	20000.00	733.0
273.15	30000.00	739.0
293.15	100.00	703.0
293.15	10000.00	711.0
293.15	20000.00	718.0
293.15	30000.00	725.0
313.15	100.00	687.0
313.15	10000.00	696.0
313.15	20000.00	704.0
313.15	30000.00	712.0
333.15	100.00	670.0
333.15	10000.00	681.0
333.15	20000.00	690.0
333.15	30000.00	698.0

Viscosity, Pa*s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Viscosity, Pa*s of Octane - Liquid
303.15	101.33	0.0005

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
298.15	100.00	698.64
298.15	2130.00	700.14
298.15	4150.00	701.87
298.15	6180.00	703.56
298.15	8210.00	705.17
298.15	10230.00	706.78
298.15	11250.00	707.58
298.15	12260.00	708.37
298.15	14290.00	709.9
298.15	16310.00	711.41
298.15	18340.00	712.9
298.15	20370.00	714.36
298.15	22390.00	715.78
298.15	24420.00	717.18
298.15	26450.00	718.56
298.15	28470.00	719.9
298.15	29490.00	720.57
298.15	30500.00	721.22
298.15	32530.00	722.53
298.15	34550.00	723.82
298.15	36580.00	725.06
298.15	38600.00	726.32
298.15	39620.00	726.94
308.15	100.00	690.43
308.15	2130.00	692.18
308.15	4150.00	694.0
308.15	6180.00	695.79
308.15	8210.00	697.53
308.15	10230.00	699.24
308.15	11250.00	700.07
308.15	12260.00	700.88
308.15	14290.00	702.55
308.15	16310.00	704.13
308.15	18340.00	705.71
308.15	20370.00	707.23
308.15	22390.00	708.76
308.15	24420.00	710.22
308.15	26450.00	711.66
308.15	28470.00	713.09
308.15	29490.00	713.77
308.15	30500.00	714.47
308.15	32530.00	715.84
308.15	34550.00	717.18
308.15	36580.00	718.5
308.15	38600.00	719.82
308.15	39620.00	720.45
318.15	100.00	682.47
318.15	2130.00	684.48
318.15	4150.00	686.45
318.15	6180.00	688.29
318.15	8210.00	690.17
318.15	10230.00	691.97
318.15	11250.00	692.85
318.15	12260.00	693.77
318.15	14290.00	695.49
318.15	16310.00	697.2
318.15	18340.00	698.86
318.15	20370.00	700.47
318.15	22390.00	702.07
318.15	24420.00	703.61
318.15	26450.00	705.13
318.15	28470.00	706.66
318.15	29490.00	707.38
318.15	30500.00	708.13
318.15	32530.00	709.54
318.15	34550.00	710.96
318.15	36580.00	712.33
318.15	38600.00	713.68
318.15	39620.00	714.38
328.15	100.00	674.53
328.15	2130.00	676.49
328.15	4150.00	678.56
328.15	6180.00	680.59
328.15	8210.00	682.57
328.15	10230.00	684.51
328.15	11250.00	685.44
328.15	12260.00	686.38
328.15	14290.00	688.23
328.15	16310.00	690.03
328.15	18340.00	691.76
328.15	20370.00	693.5
328.15	22390.00	695.17
328.15	24420.00	696.82
328.15	26450.00	698.41
328.15	28470.00	699.98
328.15	29490.00	700.75
328.15	30500.00	701.53
328.15	32530.00	703.01
328.15	34550.00	704.5
328.15	36580.00	705.96
328.15	38600.00	707.36
328.15	39620.00	708.06

Viscosity, Pa*s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Viscosity, Pa*s of Octane - Liquid
298.24	100.00	0.0005
308.72	5000.00	0.0005
308.72	10000.00	0.0005
323.93	100.00	0.0004
348.64	100.00	0.0003
349.46	5000.00	0.0003
349.46	10000.00	0.0003
394.81	5000.00	0.0002
394.81	10000.00	0.0002
436.86	5000.00	0.0002
436.86	10000.00	0.0002
467.46	5000.00	0.0001
467.46	10000.00	0.0001

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
301.84	100.00	695.24
311.89	4680.00	691.6
311.89	10642.00	697.4
316.49	100.00	683.55
329.76	100.00	672.69
340.94	100.00	663.24
358.76	100.00	648.1
367.61	5873.00	648.8
367.61	11461.00	656.2
437.97	6430.00	589.6
437.97	11084.00	599.5
516.64	5712.00	505.4
516.64	9791.00	525.2

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Pressure, kPa of Octane - Liquid	Temperature, K of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
100.00	298.15	698.7
100.00	308.15	690.8
100.00	318.15	682.8
100.00	328.15	674.5
2130.00	298.15	700.4
2130.00	308.15	692.6
2130.00	318.15	684.7
2130.00	328.15	676.6
4150.00	298.15	702.2
4150.00	308.15	694.4
4150.00	318.15	686.7
4150.00	328.15	678.7
6180.00	298.15	703.8
6180.00	308.15	696.2
6180.00	318.15	688.6
6180.00	328.15	680.7
8210.00	298.15	705.4
8210.00	308.15	698.0
8210.00	318.15	690.4
8210.00	328.15	682.6
10230.00	298.15	707.0
10230.00	308.15	699.7
10230.00	318.15	692.2
10230.00	328.15	684.6
11250.00	298.15	707.8
11250.00	308.15	700.5
11250.00	318.15	693.1
11250.00	328.15	685.5
12260.00	298.15	708.6
12260.00	308.15	701.3
12260.00	318.15	694.0
12260.00	328.15	686.4
14290.00	298.15	710.1
14290.00	308.15	703.0
14290.00	318.15	695.7
14290.00	328.15	688.3
16310.00	298.15	711.7
16310.00	308.15	704.5
16310.00	318.15	697.4
16310.00	328.15	690.1
18340.00	298.15	713.1
18340.00	308.15	706.1
18340.00	318.15	699.1
18340.00	328.15	691.8
20370.00	298.15	714.6
20370.00	308.15	707.6
20370.00	318.15	700.7
20370.00	328.15	693.6
22390.00	298.15	715.9
22390.00	308.15	709.1
22390.00	318.15	702.3
22390.00	328.15	695.2
24420.00	298.15	717.4
24420.00	308.15	710.6
24420.00	318.15	703.9
24420.00	328.15	696.9
26450.00	298.15	718.8
26450.00	308.15	712.0
26450.00	318.15	705.4
26450.00	328.15	698.5
28470.00	298.15	720.1
28470.00	308.15	713.4
28470.00	318.15	706.9
28470.00	328.15	700.0
29490.00	298.15	720.8
29490.00	308.15	714.1
29490.00	318.15	707.6
29490.00	328.15	700.8
30500.00	298.15	721.4
30500.00	308.15	714.8
30500.00	318.15	708.3
30500.00	328.15	701.6
32530.00	298.15	722.7
32530.00	308.15	716.2
32530.00	318.15	709.7
32530.00	328.15	703.0
34550.00	298.15	724.0
34550.00	308.15	717.5
34550.00	318.15	711.2
34550.00	328.15	704.5
36580.00	298.15	725.3
36580.00	308.15	718.8
36580.00	318.15	712.5
36580.00	328.15	706.0
38600.00	298.15	726.5
38600.00	308.15	720.2
38600.00	318.15	713.9
38600.00	328.15	707.4
39620.00	298.15	727.1
39620.00	308.15	720.8
39620.00	318.15	714.6
39620.00	328.15	708.1

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
288.15	100.00	706.6
288.15	5000.00	710.9
288.15	10000.00	714.7
288.15	20000.00	721.7
288.15	30000.00	728.1
288.15	40000.00	734.3
298.15	100.00	698.6
298.15	5000.00	703.4
298.15	10000.00	707.0
298.15	20000.00	714.6
298.15	30000.00	721.4
298.15	40000.00	727.7
308.15	100.00	690.5
308.15	5000.00	695.0
308.15	10000.00	699.4
308.15	20000.00	707.3
308.15	30000.00	714.5
308.15	40000.00	720.8

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
293.15	101.00	702.58
303.15	101.00	694.48
313.15	101.00	686.32
323.15	101.00	678.09
288.15	100.00	706.5
288.15	1000.00	707.2
288.15	5000.00	710.3
288.15	10000.00	714.1
288.15	15000.00	717.7
288.15	20000.00	721.2
288.15	25000.00	724.5
288.15	30000.00	727.7
288.15	35000.00	730.8
288.15	40000.00	733.7
288.15	45000.00	736.5
288.15	50000.00	739.2
288.15	55000.00	741.7
288.15	60000.00	744.1
293.15	100.00	702.5
293.15	1000.00	703.2
293.15	5000.00	706.4
293.15	10000.00	710.3
293.15	15000.00	714.0
293.15	20000.00	717.6
293.15	25000.00	721.0
293.15	30000.00	724.3
293.15	35000.00	727.5
293.15	40000.00	730.5
293.15	45000.00	733.3
293.15	50000.00	736.0
293.15	55000.00	738.6
293.15	60000.00	741.0
298.15	100.00	698.5
298.15	1000.00	699.2
298.15	5000.00	702.5
298.15	10000.00	706.5
298.15	15000.00	710.3
298.15	20000.00	714.0
298.15	25000.00	717.6
298.15	30000.00	720.9
298.15	35000.00	724.1
298.15	40000.00	727.2
298.15	45000.00	730.1
298.15	50000.00	732.9
298.15	55000.00	735.5
298.15	60000.00	738.0
303.15	100.00	694.4
303.15	1000.00	695.2
303.15	5000.00	698.6
303.15	10000.00	702.7
303.15	15000.00	706.7
303.15	20000.00	710.5
303.15	25000.00	714.1
303.15	30000.00	717.5
303.15	35000.00	720.9
303.15	40000.00	724.0
303.15	45000.00	727.0
303.15	50000.00	729.8
303.15	55000.00	732.5
303.15	60000.00	735.0
308.15	100.00	690.4
308.15	1000.00	691.2
308.15	5000.00	694.7
308.15	10000.00	698.9
308.15	15000.00	703.0
308.15	20000.00	706.9
308.15	25000.00	710.6
308.15	30000.00	714.2
308.15	35000.00	717.5
308.15	40000.00	720.8
308.15	45000.00	723.8
308.15	50000.00	726.7
308.15	55000.00	729.4
308.15	60000.00	731.9
313.15	100.00	686.3
313.15	1000.00	687.1
313.15	5000.00	690.8
313.15	10000.00	695.1
313.15	15000.00	699.3
313.15	20000.00	703.3
313.15	25000.00	707.2
313.15	30000.00	710.8
313.15	35000.00	714.3
313.15	40000.00	717.6
313.15	45000.00	720.7
313.15	50000.00	723.6
313.15	55000.00	726.3
313.15	60000.00	728.9
318.15	100.00	682.2
318.15	1000.00	683.0
318.15	5000.00	686.8
318.15	10000.00	691.3
318.15	15000.00	695.6
318.15	20000.00	699.7
318.15	25000.00	703.6
318.15	30000.00	707.4
318.15	35000.00	711.0
318.15	40000.00	714.3
318.15	45000.00	717.5
318.15	50000.00	720.5
318.15	55000.00	723.3
318.15	60000.00	725.9
323.15	100.00	678.0
323.15	1000.00	678.9
323.15	5000.00	682.8
323.15	10000.00	687.4
323.15	15000.00	691.9
323.15	20000.00	696.1
323.15	25000.00	700.2
323.15	30000.00	704.0
323.15	35000.00	707.7
323.15	40000.00	711.1
323.15	45000.00	714.4
323.15	50000.00	717.4
323.15	55000.00	720.3
323.15	60000.00	722.9
328.15	100.00	673.8
328.15	1000.00	674.7
328.15	5000.00	678.7
328.15	10000.00	683.5
328.15	15000.00	688.1
328.15	20000.00	692.5
328.15	25000.00	696.7
328.15	30000.00	700.7
328.15	35000.00	704.4
328.15	40000.00	707.9
328.15	45000.00	711.3
328.15	50000.00	714.4
328.15	55000.00	717.3
328.15	60000.00	719.9
333.15	100.00	669.7
333.15	1000.00	670.6
333.15	5000.00	674.8
333.15	10000.00	679.7
333.15	15000.00	684.5
333.15	20000.00	689.0
333.15	25000.00	693.2
333.15	30000.00	697.3
333.15	35000.00	701.1
333.15	40000.00	704.7
333.15	45000.00	708.1
333.15	50000.00	711.3
333.15	55000.00	714.2
333.15	60000.00	716.9
343.15	100.00	661.2
343.15	1000.00	662.2
343.15	5000.00	666.6
343.15	10000.00	671.9
343.15	15000.00	677.0
343.15	20000.00	681.8
343.15	25000.00	686.3
343.15	30000.00	690.6
343.15	35000.00	694.6
343.15	40000.00	698.4
343.15	45000.00	701.9
343.15	50000.00	705.2
343.15	55000.00	708.2
343.15	60000.00	711.0
353.15	100.00	652.6
353.15	1000.00	653.7
353.15	5000.00	658.4
353.15	10000.00	664.1
353.15	15000.00	669.4
353.15	20000.00	674.5
353.15	25000.00	679.3
353.15	30000.00	683.9
353.15	35000.00	688.1
353.15	40000.00	692.1
353.15	45000.00	695.7
353.15	50000.00	699.1
353.15	55000.00	702.3
353.15	60000.00	705.1
363.15	100.00	643.8
363.15	1000.00	645.0
363.15	5000.00	650.1
363.15	10000.00	656.1
363.15	15000.00	661.9
363.15	20000.00	667.3
363.15	25000.00	672.4
363.15	30000.00	677.2
363.15	35000.00	681.6
363.15	40000.00	685.8
363.15	45000.00	689.6
363.15	50000.00	693.1
363.15	55000.00	696.3
363.15	60000.00	699.2
373.15	100.00	634.7
373.15	1000.00	636.3
373.15	5000.00	641.8
373.15	10000.00	648.2
373.15	15000.00	654.4
373.15	20000.00	660.1
373.15	25000.00	665.5
373.15	30000.00	670.6
373.15	35000.00	675.3
373.15	40000.00	679.6
373.15	45000.00	683.6
373.15	50000.00	687.3
373.15	55000.00	690.5
373.15	60000.00	693.5
393.15	100.00	616.3
393.15	1000.00	618.1
393.15	5000.00	624.3
393.15	10000.00	631.8
393.15	15000.00	638.8
393.15	20000.00	645.3
393.15	25000.00	651.5
393.15	30000.00	657.1
393.15	35000.00	662.3
393.15	40000.00	667.1
393.15	45000.00	671.4
393.15	50000.00	675.3
393.15	55000.00	678.8
393.15	60000.00	681.8
413.15	1000.00	599.3
413.15	5000.00	606.6
413.15	10000.00	615.1
413.15	15000.00	623.1
413.15	20000.00	630.6
413.15	25000.00	637.4
413.15	30000.00	643.8
413.15	35000.00	649.6
413.15	40000.00	654.8
413.15	45000.00	659.5
413.15	50000.00	663.6
413.15	55000.00	667.2
413.15	60000.00	670.2

Speed of sound, m/s of Octane [ref]

Operational condition: Frequency, MHz = 1.5 (Liquid)

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Speed of sound, m/s of Octane - Liquid
283.15	100.00	1234.58
283.15	5100.00	1267.06
283.15	10100.00	1296.87
283.15	20100.00	1353.62
283.15	30100.00	1405.73
283.15	40100.00	1453.45
283.15	50100.00	1497.98
283.15	60100.00	1539.83
283.15	70100.00	1579.76
283.15	80100.00	1618.95
283.15	90100.00	1652.42
283.15	95100.00	1670.72
293.15	100.00	1193.74
293.15	5100.00	1227.94
293.15	10100.00	1259.45
293.15	20100.00	1317.25
293.15	30100.00	1370.38
293.15	40100.00	1419.61
293.15	50100.00	1465.58
293.15	60100.00	1508.42
293.15	70100.00	1549.02
293.15	80100.00	1587.34
293.15	90100.00	1623.92
293.15	95100.00	1641.84
303.15	100.00	1151.82
303.15	5100.00	1187.62
303.15	10100.00	1220.99
303.15	20100.00	1282.11
303.15	30100.00	1336.81
303.15	40100.00	1388.06
303.15	50100.00	1435.5
303.15	60100.00	1480.01
303.15	70100.00	1521.7
303.15	80100.00	1561.42
303.15	90100.00	1598.88
303.15	95100.00	1617.0
313.15	100.00	1112.07
313.15	5100.00	1148.97
313.15	10100.00	1183.44
313.15	20100.00	1247.34
313.15	30100.00	1303.76
313.15	40100.00	1356.4
313.15	50100.00	1405.08
313.15	60100.00	1450.73
313.15	70100.00	1493.22
313.15	80100.00	1533.64
313.15	90100.00	1571.88
313.15	95100.00	1590.18
323.15	100.00	1071.08
323.15	5100.00	1110.36
323.15	10100.00	1146.13
323.15	20100.00	1212.3
323.15	30100.00	1271.56
323.15	40100.00	1325.33
323.15	50100.00	1375.24
323.15	60100.00	1421.82
323.15	70100.00	1465.52
323.15	80100.00	1506.58
323.15	90100.00	1545.71
323.15	95100.00	1564.52
333.15	100.00	1030.88
333.15	5100.00	1072.38
333.15	10100.00	1110.11
333.15	20100.00	1178.21
333.15	30100.00	1239.76
333.15	40100.00	1295.04
333.15	50100.00	1346.15
333.15	60100.00	1393.88
333.15	70100.00	1438.49
333.15	80100.00	1480.2
333.15	90100.00	1519.75
333.15	95100.00	1538.99
343.15	100.00	990.7
343.15	5100.00	1034.29
343.15	10100.00	1074.24
343.15	20100.00	1144.98
343.15	30100.00	1208.69
343.15	40100.00	1265.87
343.15	50100.00	1318.0
343.15	60100.00	1367.82
343.15	70100.00	1412.81
343.15	80100.00	1455.47
343.15	90100.00	1495.95
343.15	95100.00	1515.25

Molar heat capacity at constant pressure, J/K/mol of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Molar heat capacity at constant pressure, J/K/mol of Octane - Liquid
323.15	100.00	263.30
328.15	100.00	265.70
333.15	100.00	267.98
338.15	100.00	270.38
343.15	100.00	272.66
348.15	100.00	275.18
353.15	100.00	277.58
358.15	100.00	280.09
363.15	100.00	282.60
368.15	100.00	285.11
373.15	100.00	287.86
378.15	100.00	290.37
383.15	100.00	293.45
323.15	10130.00	260.90
328.15	10130.00	263.18
333.15	10130.00	265.58
338.15	10130.00	267.75
343.15	10130.00	270.04
348.15	10130.00	272.32
353.15	10130.00	274.49
358.15	10130.00	277.00
363.15	10130.00	279.17
368.15	10130.00	281.57
373.15	10130.00	283.97
378.15	10130.00	286.49
383.15	10130.00	288.88
388.15	10130.00	290.94
393.15	10130.00	292.88
398.15	10130.00	295.97

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Pressure, kPa of Octane - Liquid	Temperature, K of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
100.00	298.15	698.71

Viscosity, Pa*s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Viscosity, Pa*s of Octane - Liquid
303.15	101.30	0.0005

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
298.15	100.00	698.58

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
293.21	1996.00	703.76
293.22	3994.00	705.71
293.22	6001.00	707.57
293.21	8004.00	709.25
293.22	10009.00	710.88
293.21	13010.00	713.21
293.22	16009.00	715.43
293.22	19011.00	717.57
293.22	22012.00	719.76
293.22	25004.00	721.88
293.22	28004.00	724.19
293.21	30002.00	725.54
313.11	2007.00	688.27
313.11	4000.00	690.26
313.10	5999.00	692.07
313.11	7997.00	693.85
313.11	10009.00	695.59
313.11	13005.00	698.26
313.11	16009.00	700.84
313.10	19006.00	703.5
313.10	21998.00	706.05
313.10	25000.00	708.39
313.10	27998.00	710.67
313.10	30001.00	712.15
333.01	2005.00	672.19
333.01	3993.00	674.49
333.01	5998.00	676.69
333.01	8014.00	678.82
333.01	10007.00	680.8
333.01	13004.00	683.6
333.01	16002.00	686.47
333.01	19006.00	689.24
333.00	22003.00	691.91
333.01	25006.00	694.49
333.01	28003.00	696.99
333.01	30012.00	698.61
353.12	2008.00	655.38
353.12	3999.00	657.99
353.12	6000.00	660.5
353.12	8001.00	663.11
353.12	10006.00	665.45
353.13	13003.00	668.83
353.13	16004.00	672.05
353.12	19000.00	674.99
353.12	22003.00	677.96
353.12	25005.00	680.81
353.12	28008.00	683.56
353.12	30004.00	685.34

Viscosity, Pa*s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Viscosity, Pa*s of Octane - Liquid
293.21	1996.00	0.0006
293.22	3994.00	0.0006
293.22	6001.00	0.0006
293.21	8004.00	0.0006
293.22	10009.00	0.0006
293.21	13010.00	0.0006
293.22	16009.00	0.0006
293.22	19011.00	0.0007
293.22	22012.00	0.0007
293.22	25004.00	0.0007
293.22	28004.00	0.0007
293.21	30002.00	0.0007
313.11	2007.00	0.0004
313.11	4000.00	0.0004
313.10	5999.00	0.0005
313.11	7997.00	0.0005
313.11	10009.00	0.0005
313.11	13005.00	0.0005
313.11	16009.00	0.0005
313.10	19006.00	0.0005
313.10	21998.00	0.0005
313.10	25000.00	0.0006
313.10	27998.00	0.0006
313.10	30001.00	0.0006
333.01	2005.00	0.0004
333.01	3993.00	0.0004
333.01	5998.00	0.0004
333.01	8014.00	0.0004
333.01	10007.00	0.0004
333.01	13004.00	0.0004
333.01	16002.00	0.0004
333.01	19006.00	0.0004
333.00	22003.00	0.0004
333.01	25006.00	0.0005
333.01	28003.00	0.0005
333.01	30012.00	0.0005
353.12	2008.00	0.0003
353.12	3999.00	0.0003
353.12	6000.00	0.0003
353.12	8001.00	0.0003
353.12	10006.00	0.0003
353.13	13003.00	0.0003
353.13	16004.00	0.0003
353.12	19000.00	0.0004
353.12	22003.00	0.0004
353.12	25005.00	0.0004
353.12	28008.00	0.0004
353.12	30004.00	0.0004

Speed of sound, m/s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Speed of sound, m/s of Octane - Liquid
296.97	100.00	1173.0
303.61	100.00	1151.7
318.37	100.00	1089.5
332.50	100.00	1029.1
347.68	100.00	970.1
362.53	100.00	912.3
377.50	100.00	855.4
391.61	100.00	806.4
297.28	4000.00	1196.5
303.53	4000.00	1172.7
318.30	4000.00	1121.2
332.26	4000.00	1066.7
347.40	4000.00	1007.2
362.28	4000.00	955.4
377.03	4000.00	909.7
390.80	4000.00	860.1
407.38	4000.00	802.1
412.59	4000.00	786.2
422.73	4000.00	747.2
431.82	4000.00	720.1
442.23	4000.00	682.1
452.55	4000.00	646.4
462.37	4000.00	614.7
472.05	4000.00	579.7
482.98	4000.00	543.0
493.41	4000.00	503.5
502.54	4000.00	477.8
513.00	4000.00	439.1
522.92	4000.00	407.7
532.23	4000.00	373.2
537.40	4000.00	354.7
542.87	4000.00	337.8
546.68	4000.00	325.7
550.42	4000.00	315.2
557.27	4000.00	290.5
561.20	4000.00	276.7
567.01	4000.00	257.3
570.16	4000.00	245.6
297.34	7000.00	1222.0
303.33	7000.00	1199.7
318.35	7000.00	1141.4
332.33	7000.00	1089.1
347.29	7000.00	1031.9
362.17	7000.00	979.6
377.33	7000.00	933.5
391.00	7000.00	892.3
407.46	7000.00	836.9
412.65	7000.00	818.8
422.88	7000.00	784.5
431.88	7000.00	754.2
442.49	7000.00	723.8
452.64	7000.00	689.9
462.45	7000.00	660.1
472.15	7000.00	631.6
483.04	7000.00	599.7
493.48	7000.00	565.4
502.73	7000.00	537.1
513.26	7000.00	506.5
523.46	7000.00	478.6
532.36	7000.00	450.6
537.75	7000.00	436.8
543.83	7000.00	422.0
547.82	7000.00	406.8
552.01	7000.00	398.1
558.19	7000.00	380.2
561.87	7000.00	372.6
566.82	7000.00	356.5
570.20	7000.00	347.6
573.03	7000.00	341.0
575.57	7000.00	332.6
578.92	7000.00	323.1
297.38	10000.00	1242.7
303.38	10000.00	1213.7
318.11	10000.00	1164.8
332.32	10000.00	1108.6
347.37	10000.00	1053.4
362.12	10000.00	1006.2
377.35	10000.00	960.5
391.09	10000.00	917.4
407.45	10000.00	865.2
412.71	10000.00	846.7
422.61	10000.00	818.2
431.92	10000.00	789.8
442.65	10000.00	755.7
452.77	10000.00	728.1
465.54	10000.00	695.8
472.28	10000.00	676.9
483.12	10000.00	646.1
493.62	10000.00	614.7
502.95	10000.00	590.5
513.46	10000.00	563.1
523.60	10000.00	533.3
532.59	10000.00	511.4
538.10	10000.00	497.5
544.52	10000.00	483.1
548.60	10000.00	471.5
552.52	10000.00	465.1
558.64	10000.00	448.0
562.27	10000.00	441.3
566.96	10000.00	430.4
570.48	10000.00	424.0
573.37	10000.00	414.0
576.28	10000.00	408.7
579.36	10000.00	400.8
297.35	12000.00	1250.8
303.42	12000.00	1233.0
318.37	12000.00	1184.5
332.56	12000.00	1128.3
347.46	12000.00	1072.7
363.67	12000.00	1027.8
379.75	12000.00	973.9
394.67	12000.00	920.8
403.71	12000.00	896.1
414.33	12000.00	864.0
422.69	12000.00	844.3
431.77	12000.00	815.2
442.73	12000.00	779.7
452.88	12000.00	750.8
462.61	12000.00	724.2
472.38	12000.00	693.8
483.14	12000.00	672.7
493.73	12000.00	645.0
503.17	12000.00	616.5
513.67	12000.00	591.5
523.17	12000.00	570.6
532.79	12000.00	545.1
538.41	12000.00	530.4
543.27	12000.00	520.1
549.27	12000.00	505.4
552.88	12000.00	500.8
559.37	12000.00	486.2
562.71	12000.00	477.8
567.10	12000.00	471.0
570.75	12000.00	461.0
573.60	12000.00	454.4
576.53	12000.00	451.3
579.57	12000.00	444.1

Speed of sound, m/s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Fluid (supercritical or subcritical phases)	Pressure, kPa of Octane - Fluid (supercritical or subcritical phases)	Speed of sound, m/s of Octane - Fluid (supercritical or subcritical phases)
573.80	3000.00	135.4
577.56	3000.00	110.1
582.19	3000.00	86.9
585.88	3000.00	88.4
589.68	3000.00	93.7
594.90	3000.00	102.1
599.12	3000.00	108.9
605.28	3000.00	116.6
610.17	3000.00	124.3
614.76	3000.00	129.2
619.43	3000.00	134.1
624.89	3000.00	139.4
630.15	3000.00	144.3
635.95	3000.00	149.3
638.90	3000.00	152.4
573.69	3500.00	189.0
577.86	3500.00	168.5
582.61	3500.00	144.9
586.85	3500.00	124.2
591.09	3500.00	108.6
596.02	3500.00	100.7
599.76	3500.00	95.6
605.73	3500.00	94.8
610.28	3500.00	103.2
614.83	3500.00	111.5
619.62	3500.00	119.0
624.55	3500.00	124.9
629.96	3500.00	132.1
635.97	3500.00	140.0
638.73	3500.00	142.4
573.05	4000.00	228.1
575.02	4000.00	217.1
579.05	4000.00	198.3
583.76	4000.00	181.0
588.01	4000.00	166.2
594.05	4000.00	140.2
598.63	4000.00	125.5
602.47	4000.00	114.3
606.87	4000.00	111.1
612.50	4000.00	108.7
617.46	4000.00	110.4
622.00	4000.00	112.6
624.66	4000.00	114.2
628.69	4000.00	120.4
632.06	4000.00	124.2
636.07	4000.00	131.6
642.66	4000.00	142.7
573.90	4500.00	250.4
577.56	4500.00	236.5
583.28	4500.00	215.8
587.72	4500.00	200.5
591.69	4500.00	186.7
597.28	4500.00	170.5
601.10	4500.00	159.7
607.11	4500.00	144.8
611.94	4500.00	133.3
616.02	4500.00	128.5
619.76	4500.00	125.2
625.00	4500.00	125.1
630.45	4500.00	126.6
636.31	4500.00	132.0
639.03	4500.00	134.5
584.07	5000.00	239.2
588.39	5000.00	226.1
593.97	5000.00	206.7
599.17	5000.00	192.7
603.01	5000.00	180.4
607.61	5000.00	169.3
613.58	5000.00	153.7
616.33	5000.00	148.3
620.31	5000.00	144.0
623.42	5000.00	141.6
625.29	5000.00	139.2
629.77	5000.00	137.3
633.13	5000.00	137.6
637.58	5000.00	140.4
642.09	5000.00	144.1
584.52	6000.00	280.5
588.83	6000.00	270.2
594.09	6000.00	255.1
599.18	6000.00	241.2
603.24	6000.00	226.2
607.97	6000.00	215.3
613.80	6000.00	204.8
623.50	6000.00	184.3
633.62	6000.00	169.8
642.28	6000.00	160.5
584.97	7000.00	314.5
589.14	7000.00	302.3
594.28	7000.00	290.8
599.55	7000.00	276.6
603.57	7000.00	254.3
608.40	7000.00	254.8
614.19	7000.00	242.3
623.84	7000.00	224.1
633.94	7000.00	204.8
642.75	7000.00	194.7
585.27	8000.00	351.8
589.41	8000.00	337.0
594.52	8000.00	322.3
599.72	8000.00	309.6
603.85	8000.00	299.0
608.86	8000.00	285.3
614.65	8000.00	273.2
624.50	8000.00	254.1
634.48	8000.00	240.7
643.16	8000.00	229.4
585.51	9000.00	367.9
589.67	9000.00	358.4
594.74	9000.00	346.5
600.00	9000.00	334.0
604.21	9000.00	324.3
609.24	9000.00	312.3
615.18	9000.00	302.0
624.87	9000.00	283.1
585.79	10000.00	392.1
589.93	10000.00	385.1
594.94	10000.00	374.1
601.00	10000.00	358.1
609.54	10000.00	340.1

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
313.15	100.00	686.05
313.15	1030.00	687.19
313.15	1950.00	688.13
313.15	2950.00	689.08
313.15	3960.00	690.0
313.15	4960.00	690.87
313.15	5970.00	691.78
313.15	6970.00	692.65
313.15	7980.00	693.54
313.15	8980.00	694.38
313.15	9990.00	695.26
313.15	11030.00	696.11
313.15	11950.00	696.94
313.15	12950.00	697.75
313.15	13960.00	698.56
313.15	14960.00	699.37
313.15	15970.00	700.18
313.15	16970.00	700.99
313.15	17980.00	701.77
313.15	18980.00	702.53
313.15	19990.00	703.31
323.15	100.00	677.56
323.15	950.00	678.99
323.15	1960.00	680.02
323.15	2970.00	681.01
323.15	3980.00	681.99
323.15	4980.00	682.97
323.15	5980.00	683.91
323.15	6990.00	684.86
323.15	7990.00	685.78
323.15	9000.00	686.69
323.15	10090.00	687.59
323.15	10950.00	688.51
323.15	11960.00	689.4
323.15	12970.00	690.29
323.15	13980.00	691.16
323.15	14980.00	691.98
323.15	15980.00	692.86
323.15	16990.00	693.68
323.15	17990.00	694.53
323.15	19000.00	695.33
323.15	20090.00	696.18
333.15	100.00	669.13
333.15	1050.00	670.67
333.15	1940.00	671.75
333.15	2950.00	672.81
333.15	3950.00	673.87
333.15	4960.00	674.91
333.15	5960.00	675.95
333.15	6960.00	676.93
333.15	7990.00	677.93
333.15	8990.00	678.93
333.15	10000.00	679.89
333.15	11050.00	680.86
333.15	11940.00	681.81
333.15	12950.00	682.71
333.15	13950.00	683.67
333.15	14960.00	684.58
333.15	15960.00	685.48
333.15	16960.00	686.34
333.15	17990.00	687.26
333.15	18990.00	688.1
333.15	20000.00	688.97
343.15	100.00	661.02
343.15	960.00	662.23
343.15	1970.00	663.39
343.15	2980.00	664.55
343.15	3980.00	665.65
343.15	4990.00	666.79
343.15	5990.00	667.86
343.15	7000.00	668.94
343.15	8010.00	670.02
343.15	9010.00	671.05
343.15	10100.00	672.12
343.15	10960.00	673.13
343.15	11970.00	674.15
343.15	12980.00	675.12
343.15	13980.00	676.13
343.15	14990.00	677.1
343.15	15990.00	678.03
343.15	17000.00	678.97
343.15	18010.00	679.93
343.15	19010.00	680.86
343.15	20100.00	681.78
353.15	100.00	652.22
353.15	1060.00	653.65
353.15	1940.00	654.91
353.15	2950.00	656.12
353.15	3960.00	657.35
353.15	4960.00	658.54
353.15	5960.00	659.71
353.15	6970.00	660.9
353.15	7980.00	662.03
353.15	8980.00	663.17
353.15	9980.00	664.24
353.15	11060.00	665.33
353.15	11940.00	666.44
353.15	12950.00	667.49
353.15	13960.00	668.52
353.15	14960.00	669.56
353.15	15960.00	670.6
353.15	16970.00	671.6
353.15	17980.00	672.57
353.15	18980.00	673.56
353.15	19980.00	674.52
363.15	100.00	643.71
363.15	950.00	644.91
363.15	1960.00	646.3
363.15	2970.00	647.63
363.15	3970.00	648.92
363.15	4980.00	650.23
363.15	5980.00	651.49
363.15	6990.00	652.73
363.15	7990.00	653.97
363.15	8990.00	655.15
363.15	10090.00	656.34
363.15	10950.00	657.54
363.15	11960.00	658.66
363.15	12970.00	659.79
363.15	13970.00	660.94
363.15	14980.00	662.01
363.15	15980.00	663.09
363.15	16990.00	664.19
363.15	17990.00	665.21
363.15	18990.00	666.28
363.15	20090.00	667.28

Thermal conductivity, W/m/K of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Thermal conductivity, W/m/K of Octane - Liquid
255.43	100.00	0.1386
255.34	5200.00	0.1409
255.48	10100.00	0.1427
255.80	20000.00	0.1458
255.12	30000.00	0.1482
274.91	100.00	0.1318
275.13	5000.00	0.1338
275.12	10200.00	0.1358
274.99	20200.00	0.1400
275.01	30200.00	0.1438
295.39	200.00	0.1265
295.22	5100.00	0.1287
295.33	10200.00	0.1309
295.18	20000.00	0.1351
295.13	30000.00	0.1391
315.13	100.00	0.1201
315.18	5000.00	0.1227
315.06	10000.00	0.1252
315.14	20200.00	0.1299
315.00	30000.00	0.1340
334.94	100.00	0.1143
334.97	5100.00	0.1170
335.05	10000.00	0.1194
334.94	20100.00	0.1245
334.94	30000.00	0.1288
355.08	100.00	0.1084
354.92	5000.00	0.1114
355.03	10000.00	0.1142
355.02	20000.00	0.1194
354.99	30000.00	0.1242
375.06	400.00	0.1019
374.87	5100.00	0.1052
375.08	10200.00	0.1082
374.90	20000.00	0.1147
375.26	30000.00	0.1198

Viscosity, Pa*s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Viscosity, Pa*s of Octane - Liquid
323.15	100.00	0.0004
323.15	10096.00	0.0004
323.15	20701.00	0.0005
323.15	30654.00	0.0005
323.15	41050.00	0.0006
323.15	54543.00	0.0006
323.15	68036.00	0.0007
348.14	100.00	0.0003
348.14	7551.00	0.0003
348.14	13680.00	0.0004
348.14	20500.00	0.0004
348.14	27466.00	0.0004
348.14	27469.00	0.0004
348.14	34305.00	0.0004
348.14	34314.00	0.0004
348.14	41226.00	0.0004
348.14	41227.00	0.0004
348.14	48070.00	0.0005
348.14	55000.00	0.0005
348.14	55004.00	0.0005
348.14	61992.00	0.0005
348.14	61994.00	0.0005
373.12	6723.00	0.0003
373.12	6724.00	0.0003
373.12	20592.00	0.0003
373.12	20599.00	0.0003
373.12	27397.00	0.0003
373.12	27402.00	0.0003
373.12	34317.00	0.0004
373.12	34324.00	0.0004
373.12	41184.00	0.0004
373.12	41207.00	0.0004
373.12	41221.00	0.0004
373.12	48024.00	0.0004
373.12	48032.00	0.0004
373.12	54853.00	0.0004
373.12	54866.00	0.0004
373.12	61686.00	0.0004
373.12	61704.00	0.0004
423.09	14725.00	0.0002
423.09	27159.00	0.0003
423.09	40831.00	0.0003
423.09	54591.00	0.0003
423.09	68420.00	0.0004

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
323.15	100.00	676.0
323.15	10096.00	687.7
323.15	20701.00	698.1
323.15	30654.00	706.7
323.15	41050.00	714.6
323.15	54543.00	723.9
323.15	68036.00	732.2
348.14	100.00	654.3
348.14	7551.00	664.7
348.14	13680.00	672.2
348.14	20500.00	679.4
348.14	27466.00	686.1
348.14	27469.00	686.1
348.14	34305.00	692.1
348.14	34314.00	690.8
348.14	41226.00	697.9
348.14	41227.00	697.8
348.14	48070.00	703.1
348.14	55000.00	708.2
348.14	55004.00	708.1
348.14	61992.00	714.2
348.14	61994.00	712.8
373.12	6723.00	644.7
373.12	6724.00	644.6
373.12	20592.00	662.9
373.12	20599.00	662.9
373.12	27397.00	670.3
373.12	27402.00	670.4
373.12	34317.00	677.1
373.12	34324.00	677.2
373.12	41184.00	683.5
373.12	41207.00	683.6
373.12	41221.00	683.6
373.12	48024.00	689.2
373.12	48032.00	689.1
373.12	54853.00	694.6
373.12	54866.00	694.6
373.12	61686.00	699.8
373.12	61704.00	699.8
423.09	14725.00	620.5
423.09	27159.00	638.8
423.09	40831.00	655.5
423.09	54591.00	668.8
423.09	68420.00	676.4

Relative permittivity at various frequencies of Octane [ref]

Operational condition: Frequency, MHz = 0.001 (Liquid)

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Relative permittivity at various frequencies of Octane - Liquid
303.07	5010.00	1.9415
303.07	10050.00	1.9487
303.07	20060.00	1.9618
303.07	25030.00	1.9682
333.25	5040.00	1.909
333.25	6780.00	1.9121
333.25	10020.00	1.9178
333.25	20050.00	1.9329
333.25	25050.00	1.9399
373.16	5040.00	1.8576
373.16	10030.00	1.8684
373.16	20030.00	1.8874
373.16	25060.00	1.8956
398.17	5010.00	1.8243
398.17	10010.00	1.8374
398.17	20050.00	1.8596
398.17	25040.00	1.8702

Viscosity, Pa*s of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Viscosity, Pa*s of Octane - Liquid
298.15	100.00	0.0005
298.15	20900.00	0.0006
298.15	40600.00	0.0008
298.15	60900.00	0.0009
298.15	80000.00	0.0010
298.15	80100.00	0.0010
298.15	100300.00	0.0012
298.15	120100.00	0.0014
298.15	139700.00	0.0016
298.15	139900.00	0.0015
298.15	159500.00	0.0018
298.15	179600.00	0.0020
298.15	197200.00	0.0022
323.15	100.00	0.0004
323.15	20100.00	0.0005
323.15	40000.00	0.0006
323.15	60600.00	0.0007
323.15	80100.00	0.0008
323.15	101000.00	0.0009
323.15	120300.00	0.0010
323.15	141500.00	0.0011
323.15	141600.00	0.0011
323.15	160300.00	0.0013
323.15	180700.00	0.0014
323.15	201800.00	0.0016
323.15	100.00	0.0004
323.15	80100.00	0.0008
348.15	100.00	0.0003
348.15	20400.00	0.0004
348.15	40800.00	0.0005
348.15	60700.00	0.0005
348.15	80100.00	0.0006
348.15	101000.00	0.0007
348.15	120400.00	0.0008
348.15	140200.00	0.0009
348.15	140300.00	0.0009
348.15	160700.00	0.0010
348.15	180800.00	0.0011
348.15	201900.00	0.0012
348.15	100.00	0.0003
348.15	80100.00	0.0006
373.15	100.00	0.0002
373.15	20600.00	0.0003
373.15	39900.00	0.0004
373.15	60000.00	0.0004
373.15	80200.00	0.0005
373.15	101100.00	0.0006
373.15	120000.00	0.0006
373.15	140900.00	0.0007
373.15	160300.00	0.0008
373.15	180500.00	0.0009
373.15	200900.00	0.0010
398.15	21600.00	0.0003
398.15	42000.00	0.0003
398.15	79400.00	0.0004
398.15	80900.00	0.0004
398.15	120900.00	0.0006
398.15	159500.00	0.0007
398.15	160200.00	0.0007
398.15	192300.00	0.0008
398.15	21600.00	0.0003
423.15	21400.00	0.0002
423.15	41100.00	0.0003
423.15	80400.00	0.0004
423.15	80700.00	0.0004
423.15	121500.00	0.0005
423.15	159700.00	0.0006
423.15	161300.00	0.0006
423.15	192500.00	0.0007
423.15	21400.00	0.0002
448.15	21000.00	0.0002
448.15	41200.00	0.0002
448.15	80500.00	0.0003
448.15	81400.00	0.0003
448.15	121500.00	0.0004
448.15	159400.00	0.0005
448.15	160300.00	0.0005
448.15	193000.00	0.0006
448.15	21000.00	0.0002
473.15	19300.00	0.0002
473.15	20000.00	0.0002
473.15	41100.00	0.0002
473.15	81100.00	0.0003
473.15	81500.00	0.0003
473.15	121100.00	0.0004
473.15	160700.00	0.0004
473.15	161300.00	0.0004
473.15	193400.00	0.0005

Mass density, kg/m3 of Octane [ref]

Fixed		Measured
Temperature, K of Octane - Liquid	Pressure, kPa of Octane - Liquid	Mass density, kg/m3 of Octane - Liquid
298.15	100.00	698.6
298.15	20900.00	715.2
298.15	40600.00	728.3
298.15	60900.00	740.0
298.15	80000.00	749.6
298.15	80100.00	749.8
298.15	100300.00	759.1
298.15	120100.00	767.3
298.15	139700.00	774.8
298.15	139900.00	774.9
298.15	159500.00	782.0
298.15	179600.00	788.7
298.15	197200.00	794.2
323.15	100.00	678.2
323.15	20100.00	697.0
323.15	40000.00	712.0
323.15	60600.00	725.0
323.15	80100.00	735.8
323.15	101000.00	746.1
323.15	120300.00	754.7
323.15	141500.00	763.4
323.15	141600.00	763.2
323.15	160300.00	770.5
323.15	180700.00	777.7
323.15	201800.00	784.8
323.15	100.00	678.2
323.15	80100.00	735.6
348.15	100.00	657.2
348.15	20400.00	679.6
348.15	40800.00	696.7
348.15	60700.00	710.6
348.15	80100.00	722.4
348.15	101000.00	733.4
348.15	120400.00	742.7
348.15	140200.00	751.2
348.15	140300.00	751.3
348.15	160700.00	759.5
348.15	180800.00	767.0
348.15	201900.00	774.3
348.15	100.00	657.2
348.15	80100.00	722.4
373.15	100.00	635.3
373.15	20600.00	662.0
373.15	39900.00	680.4
373.15	60000.00	696.0
373.15	80200.00	709.3
373.15	101100.00	721.3
373.15	120000.00	730.9
373.15	140900.00	740.6
373.15	160300.00	748.8
373.15	180500.00	756.7
373.15	200900.00	764.2
398.15	21600.00	644.4
398.15	42000.00	665.9
398.15	79400.00	694.8
398.15	80900.00	695.8
398.15	120900.00	719.0
398.15	159500.00	736.9
398.15	160200.00	737.2
398.15	192300.00	750.0
398.15	21600.00	644.6
423.15	21400.00	626.8
423.15	41100.00	650.3
423.15	80400.00	683.3
423.15	80700.00	683.5
423.15	121500.00	708.6
423.15	159700.00	727.5
423.15	161300.00	728.2
423.15	192500.00	741.1
423.15	21400.00	626.9
448.15	21000.00	607.9
448.15	41200.00	635.1
448.15	80500.00	671.0
448.15	81400.00	671.5
448.15	121500.00	697.4
448.15	159400.00	717.1
448.15	160300.00	717.5
448.15	193000.00	732.0
448.15	21000.00	608.0
473.15	19300.00	586.4
473.15	20000.00	587.7
473.15	41100.00	620.0
473.15	81100.00	659.3
473.15	81500.00	659.6
473.15	121100.00	686.7
473.15	160700.00	708.0
473.15	161300.00	708.3
473.15	193400.00	723.0

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[291.19; 425.47]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44378e+01
Coefficient B			-3.45148e+03
Coefficient C			-4.72760e+01
Temperature range, min.			291.19
Temperature range, max.			425.47
Pvap	1.33	kPa	291.19	Calculated Property
Pvap	3.01	kPa	306.11	Calculated Property
Pvap	6.23	kPa	321.03	Calculated Property
Pvap	11.96	kPa	335.95	Calculated Property
Pvap	21.52	kPa	350.87	Calculated Property
Pvap	36.66	kPa	365.79	Calculated Property
Pvap	59.53	kPa	380.71	Calculated Property
Pvap	92.74	kPa	395.63	Calculated Property
Pvap	139.32	kPa	410.55	Calculated Property
Pvap	202.67	kPa	425.47	Calculated Property
Pvap	[2.46e-03; 2417.19]	kPa	[216.38; 568.83]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.57782e+01
Coefficient B			-6.98194e+03
Coefficient C			-7.37874e+00
Coefficient D			3.38092e-06
Temperature range, min.			216.38
Temperature range, max.			568.83
Pvap	2.46e-03	kPa	216.38	Calculated Property
Pvap	0.11	kPa	255.54	Calculated Property
Pvap	1.53	kPa	294.70	Calculated Property
Pvap	10.66	kPa	333.86	Calculated Property
Pvap	46.40	kPa	373.02	Calculated Property
Pvap	145.90	kPa	412.19	Calculated Property
Pvap	364.04	kPa	451.35	Calculated Property
Pvap	767.43	kPa	490.51	Calculated Property
Pvap	1427.60	kPa	529.67	Calculated Property
Pvap	2417.19	kPa	568.83	Calculated Property

Similar Compounds

Find more compounds similar to Octane.

Mixtures

• Squalane + Octane
• Octane + Cyclohexylamine
• Octane + Ethanol, 2-ethoxy-
• Octane + o-Toluidine
• Formamide, N,N-dimethyl- + Octane
• Aniline + Octane + Water
• Octane + Cyclohexylamine + Water
• Aniline + Octane + Cyclohexylamine
• 2-Pyrrolidinone, 1-methyl- + Octane
• Hexane, tetradecafluoro- + Octane
• Octane + Perfluorooctane
• 2-Propanol, 2-methyl- + Octane
• p-Xylene + Octane
• Octane + o-Xylene
• Benzene, 1,3-dimethyl- + Octane
• Octane + Thiophene, 2-ethyl-
• Ethanol, 2-butoxy- + Octane + Water
• Methyl formate + Octane
• Ethyl formate + Octane
• Formic acid, propyl ester + Octane

Find more mixtures with Octane.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Measurements of the Liquid Viscosities of Mixtures of n-Butane, n-Hexane, and n-Octane with Squalane to 30MPa
• Thermal Conductivities of [bmim][PF6], [hmim][PF6], and [omim][PF6] from 294 to 335 K at Pressures up to 20 MPa.
• A Digital Variable-Angle Rolling-Ball Viscometer for Measurement of Viscosity, Density, and Bubble-Point Pressure of CO2 and Organic Liquid Mixtures
• Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
• Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
• An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
• Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
• Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
• (Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
• 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)
• Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
• Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
• Liquid liquid equilibria of lactam containing binary systems
• Viscosity of the binary systems 2-methyl-2-propanol with n-alkanes at T = (303.15, 308.15, 313.15, 318.15 and 323.15) K: Prediction and correlation - New UNIFAC-VISCO interaction parameters
• Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Isobaric vapor-liquid equilibrium for binary systemof 2-ethylthiophene + n-octane at 101.33 kPa
• Liquid liquid equilibria for the ternary system water + octane + 2-butyloxy-ethanol
• Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
• Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
• Application of the ionic liquid tributylmethylammonium bis(trifluoromethylsulfonyl)imide as solvent for the extraction of benzene from octane and decane at T = 298.15 K and atmospheric pressure
• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
• Isothermal and isobaric (vapour + liquid) equilibria of (alpha-pinene + n-butanol + n-octane)
• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
• Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
• Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
• (P,Vm,T) Measurements of (octane + 1-chlorohexane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
• (p,rho,T,x) and viscosity measurements of {x1 n-heptane + (1 - x1) n-octane} mixtures at high temperatures and high pressures
• Study of densities, viscosities, and speeds of sound of binary liquid mixtures of butan-1-ol with n-alkanes (C6, C8, and C10) at T = (298.15, 303.15, and 308.15) K
• Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
• p, Vm, T) measurements of (octane + benzene) at temperatures from (298.15 to 328.15) K and at pressures up to 40 MPa
• Study of molecular interactions in binary liquid mixtures of 1-octanol with n-hexane, n-octane, and n-decane using volumetric, viscometric, and acoustic properties
• The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
• Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
• Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
• The liquid-liquid coexistence curves of {x dimethyl adipate + (1 - x) n-octane} and {x dimethyl adipate + (1 - x) n-nonane} in the critical region
• Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
• Volumetric properties of dialkyl carbonate + n-alkane mixtures at high pressures: Experimental measurement and Nitta-Chao model prediction
• Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
• Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
• (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
• Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
• Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
• Determination and correlation of (liquid + liquid) equilibria of ternary and quaternary systems with octane, decane, benzene and [BMpyr][DCA] at T = 298.15 K and atmospheric pressure
• Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Densities and derived thermodynamic properties for the (n-heptane + n-octane), (n-heptane + ethanol) and (n-octane + ethanol) systems at high pressures
• Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
• Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
• Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
• Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
• Thermodynamics of mixtures containing aromatic nitriles
• Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
• Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
• DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
• Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
• The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
• Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
• A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
• Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
• Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
• Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
• The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
• Experimental Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
• Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
• Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
• Measurements of the Speed of Sound in Liquid and Supercritical n-Octane and Isooctane
• Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
• P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
• Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
• Isothermal Bubble Pressure Data for the Binary System of C2F6 and n-Octane
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
• Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
• Measurements of the Thermal Conductivity of n-Octane, Isooctane, 1-Octene, and 1-Octanol in the Temperature Range from 253 to 393 K at Pressures up to 30 MPa
• Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
• Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
• Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
• Vapor-Liquid Equilibria for the Binary Mixture alpha-Pinene + Octane
• Excess Enthalpies of the Ternary Mixtures: Diisopropyl Ether + 3-Methylpentane + (Octane or Decane) at 298.15 K
• Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
• Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
• Limiting Activity Coefficients by Comparative Tensimetry: 1-Propanol and 1-Butanol in Heptane and in Octane
• A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• Solubilities of Bis (2,2,6,6-Tetramethyl-4-Piperidinyl) Maleate in Hexane, Heptane, Octane, m-Xylene and Tetrahydrofuran from (253.15 to 310.15) K
• Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
• Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
• Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
• Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
• Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
• A Vibrating Edge Supported Plate, Fabricated by the Methods of Micro Electro Mechanical System for the Simultaneous Measurement of Density and Viscosity: Results for Methylbenzene and Octane at Temperatures between (323 and 423) K and Pressures in the Range (0.1 to 68) MPa
• Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
• Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
• Thermophysical Properties of Binary Mixtures of 2-Methyl-1-propanol with Hexane, Octane, and Decane at 298.15 K
• Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
• Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
• Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
• Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Extraction of Benzene from Aliphatic Compounds Using Commercial Ionic Liquids as Solvents: Study of the Liquid Liquid Equilibrium at T = 298.15 K
• Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
• Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
• Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
• Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
• Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
• Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
• Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
• Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
• Determination of the Relative Permittivity of Octane at Temperatures between (303 and 393) K and Pressures below 25 MPa with a Concentric Cylinder Capacitor at a Frequency of 1 kHz
• Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
• Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
• Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
• Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
• Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
• Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Densities and Viscosities of Binary Mixtures of JP-10 with n-Octane or n-Decane at Several Temperatures
• Viscosity and Density of Five Hydrocarbon Liquids at Pressures up to 200 MPa and Temperatures up to 473 K
• Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
• Analysis of Surface Tension, Density, and Speed of Sound for the Ternary Mixture Dimethyl Carbonate + p-Xylene + n-Octane
• Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
• Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
• Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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