Benzene, n-butyl- (CAS 104-51-8)

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Physical Properties

Property	Value	Unit	Source
ω	0.3930		KDB
PAff	791.90	kJ/mol	NIST
BasG	764.20	kJ/mol	NIST
Δ_cH°_liquid	[-5873.00; -5872.10]	kJ/mol
Δ_cH°_liquid	-5873.00 ± 1.10	kJ/mol	NIST
Δ_cH°_liquid	-5872.10 ± 1.10	kJ/mol	NIST
μ	0.40	debye	KDB
Δ_fG°	144.80	kJ/mol	KDB
Δ_c,grossH	5872.08	kJ/mol	KDB
Δ_c,netH	5563.967	kJ/mol	KDB
Δ_fH°_gas	[-13.82; -12.80]	kJ/mol
Δ_fH°_gas	-13.82	kJ/mol	KDB
Δ_fH°_gas	-12.80	kJ/mol	NIST
Δ_fH°_gas	-13.80 ± 1.30	kJ/mol	NIST
Δ_fH°_liquid	[-63.90; -62.90]	kJ/mol
Δ_fH°_liquid	-62.90 ± 1.20	kJ/mol	NIST
Δ_fH°_liquid	-63.90 ± 1.30	kJ/mol	NIST
Δ_fusH°	15.70	kJ/mol	Joback Calculated Property
Δ_vapH°	[50.10; 51.37]	kJ/mol
Δ_vapH°	51.37	kJ/mol	NIST
Δ_vapH°	50.80	kJ/mol	NIST
Δ_vapH°	50.10	kJ/mol	NIST
Δ_vapH°	51.00 ± 2.90	kJ/mol	NIST
Δ_vapH°	50.10	kJ/mol	NIST
IE	[8.68; 8.71]	eV
IE	8.69 ± 0.01	eV	NIST
IE	8.68	eV	NIST
IE	Outlier 8.71 ± 0.01	eV	NIST
IE	8.69	eV	NIST
IE	8.69 ± 0.01	eV	NIST
IE	8.69 ± 0.05	eV	NIST
log₁₀WS	[-4.06; -4.06]
log₁₀WS	-4.06		Aq. Solubility Prediction
log₁₀WS	-4.06		Estimated Solubility
logP_oct/wat	3.029		Crippen Calculated Property
McVol	128.000	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	2		KDB
P_c	[2887.00; 2890.00]	kPa
P_c	2890.00	kPa	KDB
P_c	2890.00 ± 40.00	kPa	NIST
P_c	2887.00 ± 7.00	kPa	NIST
ρ_c	[269.64; 269.78]	kg/m³
ρ_c	269.78 ± 5.37	kg/m³	NIST
ρ_c	269.64 ± 10.07	kg/m³	NIST
I_np	[170.00; 1078.00]
I_np	1058.00		NIST
I_np	1039.00		NIST
I_np	1043.00		NIST
I_np	1062.90		NIST
I_np	1072.40		NIST
I_np	1037.00		NIST
I_np	1037.00		NIST
I_np	1046.00		NIST
I_np	1047.00		NIST
I_np	1047.00		NIST
I_np	1036.00		NIST
I_np	1069.00		NIST
I_np	1067.00		NIST
I_np	1046.00		NIST
I_np	1048.00		NIST
I_np	1046.00		NIST
I_np	1049.00		NIST
I_np	1043.00		NIST
I_np	1039.60		NIST
I_np	1058.00		NIST
I_np	1041.00		NIST
I_np	1048.00		NIST
I_np	1054.00		NIST
I_np	1060.00		NIST
I_np	1032.30		NIST
I_np	1034.90		NIST
I_np	1048.10		NIST
I_np	1053.60		NIST
I_np	1060.00		NIST
I_np	1037.40		NIST
I_np	1029.40		NIST
I_np	1027.00		NIST
I_np	1032.30		NIST
I_np	1034.90		NIST
I_np	1037.00		NIST
I_np	1029.42		NIST
I_np	1051.00		NIST
I_np	1056.00		NIST
I_np	1059.00		NIST
I_np	1057.00		NIST
I_np	1060.00		NIST
I_np	1062.00		NIST
I_np	1063.00		NIST
I_np	1066.00		NIST
I_np	1032.00		NIST
I_np	1037.40		NIST
I_np	1035.80		NIST
I_np	1040.00		NIST
I_np	1033.00		NIST
I_np	1065.00		NIST
I_np	1033.00		NIST
I_np	1040.00		NIST
I_np	1035.20		NIST
I_np	1047.00		NIST
I_np	1068.00		NIST
I_np	1040.00		NIST
I_np	1042.00		NIST
I_np	1057.00		NIST
I_np	1040.00		NIST
I_np	1063.00		NIST
I_np	1047.40		NIST
I_np	1039.00		NIST
I_np	1044.00		NIST
I_np	1058.00		NIST
I_np	1061.00		NIST
I_np	1053.70		NIST
I_np	1053.30		NIST
I_np	1050.10		NIST
I_np	1053.70		NIST
I_np	1055.90		NIST
I_np	1036.40		NIST
I_np	1054.00		NIST
I_np	1042.00		NIST
I_np	1030.00		NIST
I_np	1043.20		NIST
I_np	1050.10		NIST
I_np	1053.70		NIST
I_np	1055.90		NIST
I_np	1053.70		NIST
I_np	1053.30		NIST
I_np	1054.00		NIST
I_np	1047.00		NIST
I_np	1041.77		NIST
I_np	1042.19		NIST
I_np	1042.00		NIST
I_np	1066.40		NIST
I_np	1056.40		NIST
I_np	1062.20		NIST
I_np	1078.00		NIST
I_np	1071.80		NIST
I_np	1074.50		NIST
I_np	1051.00		NIST
I_np	1037.42		NIST
I_np	1040.68		NIST
I_np	1043.02		NIST
I_np	1054.18		NIST
I_np	1057.89		NIST
I_np	1060.55		NIST
I_np	1040.00		NIST
I_np	1061.00		NIST
I_np	1024.00		NIST
I_np	1066.87		NIST
I_np	1044.00		NIST
I_np	1058.00		NIST
I_np	1049.00		NIST
I_np	1040.00		NIST
I_np	1044.00		NIST
I_np	1048.00		NIST
I_np	1054.00		NIST
I_np	1060.00		NIST
I_np	1042.00		NIST
I_np	1054.00		NIST
I_np	1046.00		NIST
I_np	1047.00		NIST
I_np	1047.00		NIST
I_np	1047.00		NIST
I_np	1048.00		NIST
I_np	1026.00		NIST
I_np	1038.00		NIST
I_np	1045.00		NIST
I_np	1052.00		NIST
I_np	1051.00		NIST
I_np	1053.00		NIST
I_np	1047.00		NIST
I_np	1046.00		NIST
I_np	1058.00		NIST
I_np	1052.00		NIST
I_np	1046.30		NIST
I_np	1045.00		NIST
I_np	1062.90		NIST
I_np	1069.00		NIST
I_np	1045.00		NIST
I_np	1039.00		NIST
I_np	1068.00		NIST
I_np	1067.00		NIST
I_np	1045.00		NIST
I_np	1041.00		NIST
I_np	1054.00		NIST
I_np	1058.00		NIST
I_np	1064.00		NIST
I_np	1055.00		NIST
I_np	1040.00		NIST
I_np	1022.00		NIST
I_np	1048.00		NIST
I_np	1048.00		NIST
I_np	1046.00		NIST
I_np	1047.00		NIST
I_np	1058.00		NIST
I_np	1040.00		NIST
I_np	1048.00		NIST
I_np	1047.00		NIST
I_np	1041.00		NIST
I_np	1046.00		NIST
I_np	1048.00		NIST
I_np	1036.20		NIST
I_np	1040.00		NIST
I_np	1041.00		NIST
I_np	1047.00		NIST
I_np	1033.00		NIST
I_np	Outlier 170.00		NIST
I_np	1058.00		NIST
I_np	1037.00		NIST
I_np	1036.00		NIST
I_np	1046.00		NIST
I_np	1041.00		NIST
I_np	1034.90		NIST
I_np	1029.40		NIST
I_np	1029.42		NIST
I_np	1060.00		NIST
I_np	1037.40		NIST
I_np	1033.00		NIST
I_np	1061.00		NIST
I_np	1053.70		NIST
I_np	1030.00		NIST
I_np	1042.19		NIST
I_np	1078.00		NIST
I_np	1040.68		NIST
I_np	1040.00		NIST
I	[1269.00; 1367.70]
I	1309.10		NIST
I	1356.40		NIST
I	Outlier 1362.10		NIST
I	Outlier 1367.70		NIST
I	1284.00		NIST
I	1337.60		NIST
I	1301.90		NIST
I	1284.00		NIST
I	1328.00		NIST
I	1335.00		NIST
I	1343.00		NIST
I	1321.00		NIST
I	1306.00		NIST
I	1322.00		NIST
I	1324.00		NIST
I	1325.00		NIST
I	1304.00		NIST
I	1308.00		NIST
I	1306.00		NIST
I	1280.00		NIST
I	1284.00		NIST
I	1320.00		NIST
I	1321.00		NIST
I	1332.00		NIST
I	1348.00		NIST
I	1359.00		NIST
I	1310.00		NIST
I	1284.00		NIST
I	1269.00		NIST
I	1301.00		NIST
I	1323.00		NIST
I	1271.00		NIST
I	1310.00		NIST
I	1312.00		NIST
I	1319.00		NIST
I	1310.00		NIST
I	1297.00		NIST
I	1310.00		NIST
I	1309.00		NIST
I	1284.00		NIST
I	1338.00		NIST
I	1338.00		NIST
I	1312.00		NIST
I	1309.00		NIST
I	1312.00		NIST
I	1316.00		NIST
I	1291.00		NIST
I	1310.00		NIST
I	1312.00		NIST
I	1269.00		NIST
I	1320.00		NIST
S°_gas	437.86	J/mol×K	NIST
S°_liquid	[321.21; 321.30]	J/mol×K
S°_liquid	321.21	J/mol×K	NIST
S°_liquid	321.30	J/mol×K	NIST
T_boil	[442.15; 466.00]	K
T_boil	456.46	K	KDB
T_boil	456.38	K	Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
T_boil	456.40	K	Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
T_boil	456.50	K	NIST
T_boil	456.00	K	NIST
T_boil	456.40	K	NIST
T_boil	456.43 ± 0.20	K	NIST
T_boil	454.00 ± 4.00	K	NIST
T_boil	456.60 ± 1.00	K	NIST
T_boil	456.00 ± 3.00	K	NIST
T_boil	456.41 ± 0.30	K	NIST
T_boil	455.00 ± 3.00	K	NIST
T_boil	455.70 ± 1.50	K	NIST
T_boil	456.05 ± 0.30	K	NIST
T_boil	456.50 ± 0.30	K	NIST
T_boil	456.25 ± 0.40	K	NIST
T_boil	456.41 ± 0.30	K	NIST
T_boil	456.00 ± 0.70	K	NIST
T_boil	456.42 ± 0.03	K	NIST
T_boil	456.30 ± 0.30	K	NIST
T_boil	456.41 ± 0.10	K	NIST
T_boil	456.30 ± 0.50	K	NIST
T_boil	456.41 ± 0.30	K	NIST
T_boil	456.50 ± 0.30	K	NIST
T_boil	456.25 ± 0.30	K	NIST
T_boil	456.25 ± 0.30	K	NIST
T_boil	456.50 ± 0.20	K	NIST
T_boil	456.50 ± 0.20	K	NIST
T_boil	456.34 ± 0.30	K	NIST
T_boil	455.00 ± 2.00	K	NIST
T_boil	453.00 ± 2.00	K	NIST
T_boil	455.00 ± 3.00	K	NIST
T_boil	454.50 ± 0.80	K	NIST
T_boil	456.25 ± 0.30	K	NIST
T_boil	456.41 ± 0.20	K	NIST
T_boil	456.41 ± 0.30	K	NIST
T_boil	Outlier 466.00 ± 2.00	K	NIST
T_boil	Outlier 442.15 ± 2.50	K	NIST
T_boil	453.00 ± 3.00	K	NIST
T_boil	451.00 ± 5.00	K	NIST
T_boil	457.00 ± 4.00	K	NIST
T_boil	456.45 ± 0.30	K	NIST
T_boil	453.00 ± 4.00	K	NIST
T_boil	453.00 ± 5.00	K	NIST
T_boil	456.25 ± 0.30	K	NIST
T_boil	453.65 ± 2.00	K	NIST
T_boil	453.15 ± 2.00	K	NIST
T_c	[660.05; 661.00]	K
T_c	660.50	K	KDB
T_c	660.50 ± 0.50	K	NIST
T_c	660.50	K	NIST
T_c	660.05 ± 0.50	K	NIST
T_c	660.45 ± 0.10	K	NIST
T_c	661.00 ± 0.50	K	NIST
T_fus	[184.70; 192.00]	K
T_fus	185.20	K	KDB
T_fus	185.19	K	Aq. Solubility Prediction
T_fus	185.15 ± 0.20	K	NIST
T_fus	185.15 ± 0.20	K	NIST
T_fus	185.61 ± 0.20	K	NIST
T_fus	185.61 ± 0.30	K	NIST
T_fus	185.00 ± 0.50	K	NIST
T_fus	185.18 ± 0.04	K	NIST
T_fus	185.00 ± 0.20	K	NIST
T_fus	185.18 ± 0.30	K	NIST
T_fus	184.97 ± 0.20	K	NIST
T_fus	184.70 ± 1.50	K	NIST
T_fus	184.70 ± 1.00	K	NIST
T_fus	Outlier 192.00 ± 0.30	K	NIST
T_triple	[184.60; 185.30]	K
T_triple	185.30 ± 0.01	K	NIST
T_triple	185.14 ± 0.01	K	NIST
T_triple	184.60 ± 0.25	K	NIST
V_c	[0.497; 0.497]	m³/kmol
V_c	0.497	m³/kmol	KDB
V_c	0.497	m³/kmol	NIST
Z_c	0.2615440		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[256.33; 335.30]	J/mol×K	[454.88; 659.45]

C_p,gas	256.33	J/mol×K	454.88	Joback Calculated Property
C_p,gas	271.45	J/mol×K	488.98	Joback Calculated Property
C_p,gas	285.75	J/mol×K	523.07	Joback Calculated Property
C_p,gas	299.25	J/mol×K	557.17	Joback Calculated Property
C_p,gas	311.99	J/mol×K	591.26	Joback Calculated Property
C_p,gas	323.99	J/mol×K	625.36	Joback Calculated Property
C_p,gas	335.30	J/mol×K	659.45	Joback Calculated Property
C_p,liquid	[203.00; 243.34]	J/mol×K	[293.00; 298.20]
C_p,liquid	203.00	J/mol×K	293.00	NIST
C_p,liquid	241.00	J/mol×K	298.15	NIST
C_p,liquid	243.34	J/mol×K	298.15	NIST
C_p,liquid	240.20	J/mol×K	298.20	NIST
η	[0.0007870; 0.0009010]	Pa×s	[303.15; 313.15]

η	0.0009010	Pa×s	303.15	Physical Properties of Binary Mixtures of Ethyl Formate with Benzene, Isopropyl Benzene, Isobutyl Benzene, and Butylbenzene at (303.15, 308.15, and 313.15) K
η	0.0009010	Pa×s	303.15	Density and Viscosity of Propyl Formate + Aromatic Hydrocarbons at T = (303.15, 308.15, and 313.15) K
η	0.0008440	Pa×s	308.15	Physical Properties of Binary Mixtures of Ethyl Formate with Benzene, Isopropyl Benzene, Isobutyl Benzene, and Butylbenzene at (303.15, 308.15, and 313.15) K
η	0.0008440	Pa×s	308.15	Density and Viscosity of Propyl Formate + Aromatic Hydrocarbons at T = (303.15, 308.15, and 313.15) K
η	0.0007870	Pa×s	313.15	Physical Properties of Binary Mixtures of Ethyl Formate with Benzene, Isopropyl Benzene, Isobutyl Benzene, and Butylbenzene at (303.15, 308.15, and 313.15) K
η	0.0007870	Pa×s	313.15	Density and Viscosity of Propyl Formate + Aromatic Hydrocarbons at T = (303.15, 308.15, and 313.15) K
Δ_fusH	[10.98; 11.22]	kJ/mol	[184.60; 185.30]
Δ_fusH	10.98	kJ/mol	184.60	NIST
Δ_fusH	11.22	kJ/mol	185.30	NIST
Δ_fusH	11.22	kJ/mol	185.30	NIST
Δ_vapH	[37.50; 53.50]	kJ/mol	[323.00; 456.40]

Δ_vapH	53.50	kJ/mol	323.00	NIST
Δ_vapH	48.00 ± 0.10	kJ/mol	343.00	NIST
Δ_vapH	46.80 ± 0.10	kJ/mol	358.00	NIST
Δ_vapH	46.00 ± 0.10	kJ/mol	368.00	NIST
Δ_vapH	45.20	kJ/mol	414.00	NIST
Δ_vapH	45.70	kJ/mol	416.00	NIST
Δ_vapH	47.40 ± 0.20	kJ/mol	422.00	NIST
Δ_vapH	43.50 ± 0.20	kJ/mol	422.00	NIST
Δ_vapH	40.60 ± 0.40	kJ/mol	422.00	NIST
Δ_vapH	37.50 ± 0.70	kJ/mol	422.00	NIST
Δ_vapH	39.25	kJ/mol	456.40	KDB
Δ_vapH	38.87	kJ/mol	456.40	NIST
n₀	[1.48450; 1.48950]		[293.10; 303.15]

n₀	1.48950		293.10	Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
n₀	1.48940		293.10	Extraction of Butylbenzene from Dodecane Using Hexafluorophosphate-Based Ionic Liquids: Effect of Cation Change
n₀	1.48950		293.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
n₀	1.48742		298.15	KDB
n₀	1.48735		298.15	Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
n₀	1.48740		298.15	Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
n₀	1.48450		303.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
ρ_l	[820.30; 892.80]	kg/m³	[253.15; 343.15]

ρ_l	892.60	kg/m³	253.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
ρ_l	892.80	kg/m³	253.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	864.70	kg/m³	288.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	864.47	kg/m³	288.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
ρ_l	860.00	kg/m³	293.00	KDB
ρ_l	860.60	kg/m³	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρ_l	860.17	kg/m³	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
ρ_l	860.69	kg/m³	293.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	856.68	kg/m³	298.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	856.29	kg/m³	298.15	Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
ρ_l	856.29	kg/m³	298.15	Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
ρ_l	852.65	kg/m³	303.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	852.13	kg/m³	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
ρ_l	852.56	kg/m³	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρ_l	844.07	kg/m³	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
ρ_l	844.60	kg/m³	313.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	844.50	kg/m³	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρ_l	835.98	kg/m³	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
ρ_l	836.41	kg/m³	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρ_l	836.51	kg/m³	323.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	827.86	kg/m³	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
ρ_l	828.29	kg/m³	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρ_l	828.38	kg/m³	333.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρ_l	820.30	kg/m³	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
Δ_fusS	59.50	J/mol×K	184.60	NIST
γ	[0.03; 0.03]	N/m	[293.20; 294.20]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	294.20	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.64]	kPa	[334.90; 486.52]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45284e+01
Coefficient B			-3.96130e+03
Coefficient C			-5.67370e+01
Temperature range, min.			334.90
Temperature range, max.			486.52

P_vap	1.33	kPa	334.90	Calculated Property
P_vap	3.01	kPa	351.75	Calculated Property
P_vap	6.21	kPa	368.59	Calculated Property
P_vap	11.91	kPa	385.44	Calculated Property
P_vap	21.43	kPa	402.29	Calculated Property
P_vap	36.51	kPa	419.13	Calculated Property
P_vap	59.33	kPa	435.98	Calculated Property
P_vap	92.52	kPa	452.83	Calculated Property
P_vap	139.13	kPa	469.67	Calculated Property
P_vap	202.64	kPa	486.52	Calculated Property
P_vap	[8.50e-08; 2894.10]	kPa	[185.30; 660.55]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			1.12433e+02
Coefficient B			-1.01044e+04
Coefficient C			-1.42573e+01
Coefficient D			7.81134e-06
Temperature range, min.			185.30
Temperature range, max.			660.55

P_vap	8.50e-08	kPa	185.30	Calculated Property
P_vap	5.07e-04	kPa	238.11	Calculated Property
P_vap	0.08	kPa	290.91	Calculated Property
P_vap	2.01	kPa	343.72	Calculated Property
P_vap	17.83	kPa	396.52	Calculated Property
P_vap	84.94	kPa	449.33	Calculated Property
P_vap	274.55	kPa	502.13	Calculated Property
P_vap	692.53	kPa	554.94	Calculated Property
P_vap	1489.29	kPa	607.74	Calculated Property
P_vap	2894.10	kPa	660.55	Calculated Property

Similar Compounds

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Mixtures

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Sources

KDB Vapor Pressure Data
Crippen Method
Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
Phase equilibria of (CO2 + butylbenzene) and (CO2 + butylcyclohexane) at temperatures between (323.15 and 423.15) K and at pressures up to 21MPa
Evaluation of 1-ethyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate as solvents for extraction of alkylbenzenes from hexadecane at 313 and 333 K
Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
Effect of Solvent Cation Alkyl-Chain Length on the Separation of Butylbenzene from n-Tetradecane Using Hexafluorophosphate-Based Ionic Liquids at (313.15 and 333.15) K and 101.3 kPa
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
Extraction of Butylbenzene from Dodecane Using Hexafluorophosphate-Based Ionic Liquids: Effect of Cation Change
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
Physical Properties of Binary Mixtures of Ethyl Formate with Benzene, Isopropyl Benzene, Isobutyl Benzene, and Butylbenzene at (303.15, 308.15, and 313.15) K
Density and Viscosity of Propyl Formate + Aromatic Hydrocarbons at T = (303.15, 308.15, and 313.15) K
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure

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Chemical Properties of Benzene, n-butyl- (CAS 104-51-8)