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

InChI

InChI=1S/C10H14/c1-2-3-7-10-8-5-4-6-9-10/h4-6,8-9H,2-3,7H2,1H3

InChI Key

OCKPCBLVNKHBMX-UHFFFAOYSA-N

Formula

C10H14

SMILES

CCCCc1ccccc1

Molecular Weight¹

134.22

CAS

104-51-8

Other Names

• 1-butylbenzene
• 1-phenylbutane
• UN 2709
• benzene, butyl-
• butylbenzene
• n-butylbenzene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3920; 0.3930]
ω	0.3920		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3923		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.3930		ChemSep v8.3 pure component data Compiled value
ω	0.3930		KDB
PAff	791.90	kJ/mol	NIST
BasG	764.20	kJ/mol	NIST
ΔcH°liquid	[-5873.00; -5872.10]	kJ/mol
ΔcH°liquid	-5873.00 ± 1.10	kJ/mol	NIST
ΔcH°liquid	-5872.10 ± 1.10	kJ/mol	NIST
μ	[0.37; 0.40]	debye
μ	0.37	debye	ChemSep v8.3 pure component data Compiled value
μ	0.40	debye	KDB
ΔfG°	[144.80; 145.40]	kJ/mol
ΔfG°	145.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	144.80	kJ/mol	KDB
Δc,grossH	5872.08	kJ/mol	KDB
Δc,netH	5563.967	kJ/mol	KDB
ΔfH°gas	[-13.82; -12.80]	kJ/mol
ΔfH°gas	-13.14	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-13.82	kJ/mol	KDB
ΔfH°gas	-12.80	kJ/mol	NIST
ΔfH°gas	-13.80 ± 1.30	kJ/mol	NIST
ΔfH°liquid	[-63.90; -62.90]	kJ/mol
ΔfH°liquid	-62.90 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-63.90 ± 1.30	kJ/mol	NIST
ΔfusH°	15.70	kJ/mol	Joback Calculated Property
ΔvapH°	[50.10; 51.37]	kJ/mol
ΔvapH°	51.37	kJ/mol	NIST
ΔvapH°	50.80	kJ/mol	NIST
ΔvapH°	50.10	kJ/mol	NIST
ΔvapH°	51.00 ± 2.90	kJ/mol	NIST
ΔvapH°	50.10	kJ/mol	NIST
ΔvapH°	51.00 ± 2.90	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
logPoct/wat	3.029		Crippen Calculated Property
McVol	128.000	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	2		KDB
Pc	[2886.83; 2890.00]	kPa
Pc	2890.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Pc	2887.76	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2886.83	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2890.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2890.00	kPa	KDB
Pc	2890.00 ± 40.00	kPa	NIST
Pc	2887.00 ± 7.00	kPa	NIST
Ptriple	1.54e-07	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[269.64; 269.78]	kg/m3
ρc	269.78 ± 5.37	kg/m3	NIST
ρc	269.64 ± 10.07	kg/m3	NIST
Inp	[170.00; 1078.00]
Inp	1061.00		NIST
Inp	1058.00		NIST
Inp	1039.00		NIST
Inp	1043.00		NIST
Inp	1062.90		NIST
Inp	1072.40		NIST
Inp	1037.00		NIST
Inp	1046.00		NIST
Inp	1047.00		NIST
Inp	1047.00		NIST
Inp	1036.00		NIST
Inp	1069.00		NIST
Inp	1067.00		NIST
Inp	1046.00		NIST
Inp	1048.00		NIST
Inp	1049.00		NIST
Inp	1043.00		NIST
Inp	1039.60		NIST
Inp	1058.00		NIST
Inp	1041.00		NIST
Inp	1048.00		NIST
Inp	1054.00		NIST
Inp	1060.00		NIST
Inp	1032.30		NIST
Inp	1034.90		NIST
Inp	1048.10		NIST
Inp	1053.60		NIST
Inp	1060.00		NIST
Inp	1037.40		NIST
Inp	1029.40		NIST
Inp	1027.00		NIST
Inp	1032.30		NIST
Inp	1034.90		NIST
Inp	1037.00		NIST
Inp	1029.42		NIST
Inp	1051.00		NIST
Inp	1056.00		NIST
Inp	1059.00		NIST
Inp	1057.00		NIST
Inp	1060.00		NIST
Inp	1062.00		NIST
Inp	1063.00		NIST
Inp	1066.00		NIST
Inp	1032.00		NIST
Inp	1037.40		NIST
Inp	1035.80		NIST
Inp	1040.00		NIST
Inp	1033.00		NIST
Inp	1065.00		NIST
Inp	1033.00		NIST
Inp	1040.00		NIST
Inp	1035.20		NIST
Inp	1047.00		NIST
Inp	1068.00		NIST
Inp	1040.00		NIST
Inp	1042.00		NIST
Inp	1057.00		NIST
Inp	1040.00		NIST
Inp	1063.00		NIST
Inp	1047.40		NIST
Inp	1039.00		NIST
Inp	1044.00		NIST
Inp	1058.00		NIST
Inp	1061.00		NIST
Inp	1053.70		NIST
Inp	1053.30		NIST
Inp	1050.10		NIST
Inp	1055.90		NIST
Inp	1036.40		NIST
Inp	1054.00		NIST
Inp	1042.00		NIST
Inp	1030.00		NIST
Inp	1043.20		NIST
Inp	1050.10		NIST
Inp	1053.70		NIST
Inp	1055.90		NIST
Inp	1053.30		NIST
Inp	1054.00		NIST
Inp	1047.00		NIST
Inp	1041.77		NIST
Inp	1042.19		NIST
Inp	1042.00		NIST
Inp	1066.40		NIST
Inp	1056.40		NIST
Inp	1062.20		NIST
Inp	1078.00		NIST
Inp	1071.80		NIST
Inp	1074.50		NIST
Inp	1051.00		NIST
Inp	1037.42		NIST
Inp	1040.68		NIST
Inp	1043.02		NIST
Inp	1054.18		NIST
Inp	1057.89		NIST
Inp	1060.55		NIST
Inp	1040.00		NIST
Inp	1061.00		NIST
Inp	1024.00		NIST
Inp	1066.87		NIST
Inp	1044.00		NIST
Inp	1058.00		NIST
Inp	1049.00		NIST
Inp	1040.00		NIST
Inp	1044.00		NIST
Inp	1048.00		NIST
Inp	1054.00		NIST
Inp	1060.00		NIST
Inp	1042.00		NIST
Inp	1054.00		NIST
Inp	1046.00		NIST
Inp	1047.00		NIST
Inp	1048.00		NIST
Inp	1026.00		NIST
Inp	1038.00		NIST
Inp	1045.00		NIST
Inp	1052.00		NIST
Inp	1051.00		NIST
Inp	1053.00		NIST
Inp	1047.00		NIST
Inp	1046.00		NIST
Inp	1058.00		NIST
Inp	1052.00		NIST
Inp	1046.30		NIST
Inp	1045.00		NIST
Inp	1062.90		NIST
Inp	1069.00		NIST
Inp	1045.00		NIST
Inp	1039.00		NIST
Inp	1068.00		NIST
Inp	1067.00		NIST
Inp	1045.00		NIST
Inp	1041.00		NIST
Inp	1054.00		NIST
Inp	1058.00		NIST
Inp	1064.00		NIST
Inp	1055.00		NIST
Inp	1040.00		NIST
Inp	1022.00		NIST
Inp	1048.00		NIST
Inp	1048.00		NIST
Inp	1046.00		NIST
Inp	1047.00		NIST
Inp	1058.00		NIST
Inp	1040.00		NIST
Inp	1048.00		NIST
Inp	1047.00		NIST
Inp	1041.00		NIST
Inp	1046.00		NIST
Inp	1048.00		NIST
Inp	1036.20		NIST
Inp	1040.00		NIST
Inp	1041.00		NIST
Inp	1047.00		NIST
Inp	1033.00		NIST
Inp	Outlier 170.00		NIST
Inp	1058.00		NIST
Inp	1037.00		NIST
Inp	1036.00		NIST
Inp	1046.00		NIST
Inp	1041.00		NIST
Inp	1034.90		NIST
Inp	1029.40		NIST
Inp	1029.42		NIST
Inp	1060.00		NIST
Inp	1037.40		NIST
Inp	1033.00		NIST
Inp	1053.70		NIST
Inp	1030.00		NIST
Inp	1042.19		NIST
Inp	1078.00		NIST
Inp	1040.68		NIST
Inp	1040.00		NIST
Ip	[1269.00; 1367.70]
Ip	1309.10		NIST
Ip	1356.40		NIST
Ip	Outlier 1362.10		NIST
Ip	Outlier 1367.70		NIST
Ip	1284.00		NIST
Ip	1337.60		NIST
Ip	1301.90		NIST
Ip	1284.00		NIST
Ip	1328.00		NIST
Ip	1335.00		NIST
Ip	1343.00		NIST
Ip	1321.00		NIST
Ip	1306.00		NIST
Ip	1322.00		NIST
Ip	1324.00		NIST
Ip	1325.00		NIST
Ip	1304.00		NIST
Ip	1308.00		NIST
Ip	1306.00		NIST
Ip	1280.00		NIST
Ip	1284.00		NIST
Ip	1320.00		NIST
Ip	1321.00		NIST
Ip	1332.00		NIST
Ip	1348.00		NIST
Ip	1359.00		NIST
Ip	1310.00		NIST
Ip	1284.00		NIST
Ip	1269.00		NIST
Ip	1301.00		NIST
Ip	1323.00		NIST
Ip	1271.00		NIST
Ip	1310.00		NIST
Ip	1312.00		NIST
Ip	1319.00		NIST
Ip	1310.00		NIST
Ip	1297.00		NIST
Ip	1310.00		NIST
Ip	1309.00		NIST
Ip	1284.00		NIST
Ip	1338.00		NIST
Ip	1338.00		NIST
Ip	1312.00		NIST
Ip	1309.00		NIST
Ip	1312.00		NIST
Ip	1316.00		NIST
Ip	1291.00		NIST
Ip	1320.00		NIST
Ip	1310.00		NIST
Ip	1312.00		NIST
Ip	1269.00		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
Tboil	[442.15; 466.00]	K
Tboil	456.38	K	Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
Tboil	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
Tboil	456.42	K	ChemSep v8.3 pure component data Compiled value
Tboil	456.46	K	KDB
Tboil	456.50	K	NIST
Tboil	456.00	K	NIST
Tboil	456.40	K	NIST
Tboil	456.43 ± 0.20	K	NIST
Tboil	454.00 ± 4.00	K	NIST
Tboil	456.60 ± 1.00	K	NIST
Tboil	456.00 ± 3.00	K	NIST
Tboil	456.41 ± 0.30	K	NIST
Tboil	455.00 ± 3.00	K	NIST
Tboil	455.70 ± 1.50	K	NIST
Tboil	456.05 ± 0.30	K	NIST
Tboil	456.50 ± 0.30	K	NIST
Tboil	456.25 ± 0.40	K	NIST
Tboil	456.41 ± 0.30	K	NIST
Tboil	456.00 ± 0.70	K	NIST
Tboil	456.42 ± 0.03	K	NIST
Tboil	456.30 ± 0.30	K	NIST
Tboil	456.41 ± 0.10	K	NIST
Tboil	456.30 ± 0.50	K	NIST
Tboil	456.41 ± 0.30	K	NIST
Tboil	456.50 ± 0.30	K	NIST
Tboil	456.25 ± 0.30	K	NIST
Tboil	456.25 ± 0.30	K	NIST
Tboil	456.50 ± 0.20	K	NIST
Tboil	456.50 ± 0.20	K	NIST
Tboil	456.34 ± 0.30	K	NIST
Tboil	455.00 ± 2.00	K	NIST
Tboil	453.00 ± 2.00	K	NIST
Tboil	455.00 ± 3.00	K	NIST
Tboil	454.50 ± 0.80	K	NIST
Tboil	456.25 ± 0.30	K	NIST
Tboil	456.41 ± 0.20	K	NIST
Tboil	456.41 ± 0.30	K	NIST
Tboil	Outlier 466.00 ± 2.00	K	NIST
Tboil	Outlier 442.15 ± 2.50	K	NIST
Tboil	453.00 ± 3.00	K	NIST
Tboil	451.00 ± 5.00	K	NIST
Tboil	457.00 ± 4.00	K	NIST
Tboil	456.45 ± 0.30	K	NIST
Tboil	453.00 ± 4.00	K	NIST
Tboil	453.00 ± 5.00	K	NIST
Tboil	456.25 ± 0.30	K	NIST
Tboil	453.65 ± 2.00	K	NIST
Tboil	453.15 ± 2.00	K	NIST
Tc	[660.05; 661.00]	K
Tc	660.30	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	660.50	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Tc	660.50	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	660.54	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	660.50	K	ChemSep v8.3 pure component data Compiled value
Tc	660.50	K	KDB
Tc	660.50 ± 0.50	K	NIST
Tc	660.50	K	NIST
Tc	Outlier 660.05 ± 0.50	K	NIST
Tc	660.45 ± 0.10	K	NIST
Tc	Outlier 661.00 ± 0.50	K	NIST
Tfus	[184.70; 192.00]	K
Tfus	185.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	185.30	K	ChemSep v8.3 pure component data Compiled value
Tfus	185.20	K	KDB
Tfus	185.19	K	Aq. Solubility Prediction
Tfus	185.15 ± 0.20	K	NIST
Tfus	185.15 ± 0.20	K	NIST
Tfus	185.61 ± 0.20	K	NIST
Tfus	185.61 ± 0.30	K	NIST
Tfus	185.00 ± 0.50	K	NIST
Tfus	185.18 ± 0.04	K	NIST
Tfus	185.00 ± 0.20	K	NIST
Tfus	185.18 ± 0.30	K	NIST
Tfus	184.97 ± 0.20	K	NIST
Tfus	184.70 ± 1.50	K	NIST
Tfus	184.70 ± 1.00	K	NIST
Tfus	Outlier 192.00 ± 0.30	K	NIST
Ttriple	[184.60; 185.30]	K
Ttriple	185.30	K	ChemSep v8.3 pure component data Compiled value
Ttriple	185.30 ± 0.01	K	NIST
Ttriple	185.14 ± 0.01	K	NIST
Ttriple	184.60 ± 0.25	K	NIST
Ttriple	185.30 ± 0.01	K	NIST
Ttriple	185.14 ± 0.01	K	NIST
Ttriple	184.60 ± 0.25	K	NIST
UQi	4.59		ChemSep v8.3 pure component data Compiled value
URi	5.95		ChemSep v8.3 pure component data Compiled value
Vc	[0.497; 0.497]	m3/kmol
Vc	0.497	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Vc	0.497	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.497	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.497	m3/kmol	KDB
Vc	0.497	m3/kmol	NIST
Zc	[0.2615440; 0.2620000]
Zc	0.2620000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Zc	0.2620000		ChemSep v8.3 pure component data Compiled value
Zc	0.2615440		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[203.00; 243.34]	J/mol×K	[293.00; 298.20]
Cp,liquid	203.00	J/mol×K	293.00	NIST
Cp,liquid	241.00	J/mol×K	298.15	NIST
Cp,liquid	243.34	J/mol×K	298.15	NIST
Cp,liquid	240.20	J/mol×K	298.20	NIST
Csat	[259.10; 293.90]	J/mol×K	[332.20; 401.30]
Csat	259.10	J/mol×K	332.20	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat	263.00	J/mol×K	342.10	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat	267.80	J/mol×K	354.90	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat	272.90	J/mol×K	361.80	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat	277.60	J/mol×K	371.60	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat	283.90	J/mol×K	381.50	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat	288.00	J/mol×K	391.40	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat	293.90	J/mol×K	401.30	Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
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
ΔfusH	[10.98; 11.22]	kJ/mol	[184.60; 185.30]
ΔfusH	10.98	kJ/mol	184.60	NIST
ΔfusH	10.98	kJ/mol	184.60	NIST
ΔfusH	11.22	kJ/mol	185.30	NIST
ΔfusH	11.22	kJ/mol	185.30	NIST
ΔvapH	[37.50; 53.50]	kJ/mol	[323.00; 456.40]
ΔvapH	53.50	kJ/mol	323.00	NIST
ΔvapH	48.00 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	46.80 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	46.00 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	45.20	kJ/mol	414.00	NIST
ΔvapH	45.70	kJ/mol	416.00	NIST
ΔvapH	47.40 ± 0.20	kJ/mol	422.00	NIST
ΔvapH	43.50 ± 0.20	kJ/mol	422.00	NIST
ΔvapH	40.60 ± 0.40	kJ/mol	422.00	NIST
ΔvapH	37.50 ± 0.70	kJ/mol	422.00	NIST
ΔvapH	39.25	kJ/mol	456.40	KDB
ΔvapH	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	1.48735		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	1.48742		298.15	KDB
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
ρl	[820.30; 892.80]	kg/m3	[253.15; 343.15]
ρl	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
ρl	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
ρl	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
ρl	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
ρl	860.00	kg/m3	293.00	KDB
ρl	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
ρl	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)
ρl	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
ρl	856.29	kg/m3	298.15	Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
ρl	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
ρl	856.29	kg/m3	298.15	Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
ρl	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
ρl	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
ρl	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)
ρl	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
ρl	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)
ρl	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
ρl	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
ρl	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
ρl	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)
ρl	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
ρl	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
ρl	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)
ρl	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)
ΔfusS	[59.50; 59.50]	J/mol×K	[184.60; 184.60]
ΔfusS	59.50	J/mol×K	184.60	NIST
ΔfusS	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
Cp,gas	[125.56; 484.61]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			9.74230e+01
Coefficient B			-6.19620e+02
Coefficient C			6.44224e+00
Coefficient D			-3.28160e-05
Coefficient E			-9.35020e-09
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	125.56	J/mol×K	200.00	Calculated Property
Cp,gas	200.03	J/mol×K	344.44	Calculated Property
Cp,gas	270.99	J/mol×K	488.89	Calculated Property
Cp,gas	327.72	J/mol×K	633.33	Calculated Property
Cp,gas	371.77	J/mol×K	777.78	Calculated Property
Cp,gas	406.06	J/mol×K	922.22	Calculated Property
Cp,gas	432.95	J/mol×K	1066.67	Calculated Property
Cp,gas	454.22	J/mol×K	1211.11	Calculated Property
Cp,gas	471.13	J/mol×K	1355.56	Calculated Property
Cp,gas	484.61	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[205.63; 293.00]	J/mol×K	[185.30; 400.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.73590e+02
Coefficient B			1.15140e+02
Coefficient C			5.42345e-01
Coefficient D			1.46310e-02
Coefficient E			-1.18750e-05
Temperature range, min.			185.30
Temperature range, max.			400.00
Cp,liquid	205.63	J/mol×K	185.30	Calculated Property
Cp,liquid	211.44	J/mol×K	209.16	Calculated Property
Cp,liquid	218.33	J/mol×K	233.01	Calculated Property
Cp,liquid	226.33	J/mol×K	256.87	Calculated Property
Cp,liquid	235.39	J/mol×K	280.72	Calculated Property
Cp,liquid	245.47	J/mol×K	304.58	Calculated Property
Cp,liquid	256.46	J/mol×K	328.43	Calculated Property
Cp,liquid	268.20	J/mol×K	352.29	Calculated Property
Cp,liquid	280.47	J/mol×K	376.14	Calculated Property
Cp,liquid	293.00	J/mol×K	400.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0102926; 0.0002386]	Pa×s	[200.00; 456.46]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.88290e+01
Coefficient B			1.73770e+03
Coefficient C			1.03850e+00
Coefficient D			1.54680e-06
Coefficient E			2.00000e+00
Temperature range, min.			200.00
Temperature range, max.			456.46
η	0.0102926	Pa×s	200.00	Calculated Property
η	0.0040760	Pa×s	228.50	Calculated Property
η	0.0020245	Pa×s	256.99	Calculated Property
η	0.0011776	Pa×s	285.49	Calculated Property
η	0.0007682	Pa×s	313.98	Calculated Property
η	0.0005461	Pa×s	342.48	Calculated Property
η	0.0004147	Pa×s	370.97	Calculated Property
η	0.0003317	Pa×s	399.47	Calculated Property
η	0.0002766	Pa×s	427.96	Calculated Property
η	0.0002386	Pa×s	456.46	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[57.20; 0.00]	kJ/mol	[185.30; 660.50]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			6.56980e+01
Coefficient B			3.08420e-01
Coefficient C			6.70620e-01
Coefficient D			-1.11350e+00
Coefficient E			5.32760e-01
Critical temperature, Tc (K)			6.60500e+02
Temperature range, min.			185.30
Temperature range, max.			660.50
ΔvapH	57.20	kJ/mol	185.30	Calculated Property
ΔvapH	54.20	kJ/mol	238.10	Calculated Property
ΔvapH	51.09	kJ/mol	290.90	Calculated Property
ΔvapH	47.87	kJ/mol	343.70	Calculated Property
ΔvapH	44.49	kJ/mol	396.50	Calculated Property
ΔvapH	40.84	kJ/mol	449.30	Calculated Property
ΔvapH	36.65	kJ/mol	502.10	Calculated Property
ΔvapH	31.45	kJ/mol	554.90	Calculated Property
ΔvapH	24.05	kJ/mol	607.70	Calculated Property
ΔvapH	0.00	kJ/mol	660.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[334.90; 486.52]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
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
Pvap	1.33	kPa	334.90	Calculated Property
Pvap	3.01	kPa	351.75	Calculated Property
Pvap	6.21	kPa	368.59	Calculated Property
Pvap	11.91	kPa	385.44	Calculated Property
Pvap	21.43	kPa	402.29	Calculated Property
Pvap	36.51	kPa	419.13	Calculated Property
Pvap	59.33	kPa	435.98	Calculated Property
Pvap	92.52	kPa	452.83	Calculated Property
Pvap	139.13	kPa	469.67	Calculated Property
Pvap	202.64	kPa	486.52	Calculated Property
Pvap	[1.69e-07; 2880.46]	kPa	[185.30; 660.50]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			9.32022e+01
Coefficient B			-9.18660e+03
Coefficient C			-1.13790e+01
Coefficient D			5.85850e-06
Coefficient E			2.00000e+00
Temperature range, min.			185.30
Temperature range, max.			660.50
Pvap	1.69e-07	kPa	185.30	Calculated Property
Pvap	6.61e-04	kPa	238.10	Calculated Property
Pvap	0.09	kPa	290.90	Calculated Property
Pvap	2.04	kPa	343.70	Calculated Property
Pvap	17.76	kPa	396.50	Calculated Property
Pvap	84.69	kPa	449.30	Calculated Property
Pvap	275.65	kPa	502.10	Calculated Property
Pvap	698.72	kPa	554.90	Calculated Property
Pvap	1499.70	kPa	607.70	Calculated Property
Pvap	2880.46	kPa	660.50	Calculated Property
Pvap	[8.50e-08; 2894.10]	kPa	[185.30; 660.55]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.12433e+02
Coefficient B			-1.01044e+04
Coefficient C			-1.42573e+01
Coefficient D			7.81134e-06
Coefficient E			0.00000e+00
Temperature range, min.			185.30
Temperature range, max.			660.55
Pvap	8.50e-08	kPa	185.30	Calculated Property
Pvap	5.07e-04	kPa	238.11	Calculated Property
Pvap	0.08	kPa	290.91	Calculated Property
Pvap	2.01	kPa	343.72	Calculated Property
Pvap	17.83	kPa	396.52	Calculated Property
Pvap	84.94	kPa	449.33	Calculated Property
Pvap	274.55	kPa	502.13	Calculated Property
Pvap	692.53	kPa	554.94	Calculated Property
Pvap	1489.29	kPa	607.74	Calculated Property
Pvap	2894.10	kPa	660.55	Calculated Property
Pvap	[6.40; 103.99]	kPa	[369.38; 457.48]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40644e+01
Coefficient B			-3.63340e+03
Coefficient C			-7.17720e+01
Reference			Forziati, Norris, et al., 1949, 2
Temperature range, min.			369.38
Temperature range, max.			457.48
Pvap	6.40	kPa	369.38	Calculated Property
Pvap	9.44	kPa	379.17	Calculated Property
Pvap	13.59	kPa	388.96	Calculated Property
Pvap	19.15	kPa	398.75	Calculated Property
Pvap	26.45	kPa	408.54	Calculated Property
Pvap	35.87	kPa	418.32	Calculated Property
Pvap	47.85	kPa	428.11	Calculated Property
Pvap	62.84	kPa	437.90	Calculated Property
Pvap	81.37	kPa	447.69	Calculated Property
Pvap	103.99	kPa	457.48	Calculated Property
Pvap	[6.40; 103.99]	kPa	[369.38; 457.48]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40644e+01
Coefficient B			-3.63340e+03
Coefficient C			-7.17720e+01
Reference			Forziati, Norris, et al., 1949
Temperature range, min.			369.38
Temperature range, max.			457.48
Pvap	6.40	kPa	369.38	Calculated Property
Pvap	9.44	kPa	379.17	Calculated Property
Pvap	13.59	kPa	388.96	Calculated Property
Pvap	19.15	kPa	398.75	Calculated Property
Pvap	26.45	kPa	408.54	Calculated Property
Pvap	35.87	kPa	418.32	Calculated Property
Pvap	47.85	kPa	428.11	Calculated Property
Pvap	62.84	kPa	437.90	Calculated Property
Pvap	81.37	kPa	447.69	Calculated Property
Pvap	103.99	kPa	457.48	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[944.74; 269.73]	kg/m3	[183.15; 660.50]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.79788e+01
Coefficient B			2.52030e-01
Coefficient C			6.60500e+02
Coefficient D			2.92030e-01
Temperature range, min.			183.15
Temperature range, max.			660.50
ρl	944.74	kg/m3	183.15	Calculated Property
ρl	905.54	kg/m3	236.19	Calculated Property
ρl	864.55	kg/m3	289.23	Calculated Property
ρl	821.34	kg/m3	342.27	Calculated Property
ρl	775.26	kg/m3	395.31	Calculated Property
ρl	725.31	kg/m3	448.34	Calculated Property
ρl	669.74	kg/m3	501.38	Calculated Property
ρl	605.06	kg/m3	554.42	Calculated Property
ρl	521.80	kg/m3	607.46	Calculated Property
ρl	269.73	kg/m3	660.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[185.15; 456.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.92779e-02
Coefficient B			-1.02500e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			185.15
Temperature range, max.			456.15
γ	0.04	N/m	185.15	Calculated Property
γ	0.04	N/m	215.26	Calculated Property
γ	0.03	N/m	245.37	Calculated Property
γ	0.03	N/m	275.48	Calculated Property
γ	0.03	N/m	305.59	Calculated Property
γ	0.02	N/m	335.71	Calculated Property
γ	0.02	N/m	365.82	Calculated Property
γ	0.02	N/m	395.93	Calculated Property
γ	0.02	N/m	426.04	Calculated Property
γ	0.01	N/m	456.15	Calculated Property
γ	[0.04; 1.15e-05]	N/m	[185.30; 654.32]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-7.77090e-03
Coefficient B			3.92180e+01
Coefficient C			-3.14020e+00
Coefficient D			3.96890e-04
Coefficient E			-4.75390e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 660.5 K.
Temperature range, min.			185.30
Temperature range, max.			654.32
γ	0.04	N/m	185.30	Calculated Property
γ	0.04	N/m	237.41	Calculated Property
γ	0.03	N/m	289.53	Calculated Property
γ	0.02	N/m	341.64	Calculated Property
γ	0.02	N/m	393.75	Calculated Property
γ	0.01	N/m	445.87	Calculated Property
γ	0.01	N/m	497.98	Calculated Property
γ	0.01	N/m	550.10	Calculated Property
γ	0.00	N/m	602.21	Calculated Property
γ	1.15e-05	N/m	654.32	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.07]	W/m×K	[185.30; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.92250e-01
Coefficient B			-1.10930e-03
Coefficient C			-1.56740e+02
Coefficient D			1.71240e+06
Temperature range, min.			185.30
Temperature range, max.			1000.00
λgas	0.00	W/m×K	185.30	Calculated Property
λgas	0.01	W/m×K	275.82	Calculated Property
λgas	0.01	W/m×K	366.34	Calculated Property
λgas	0.02	W/m×K	456.87	Calculated Property
λgas	0.03	W/m×K	547.39	Calculated Property
λgas	0.04	W/m×K	637.91	Calculated Property
λgas	0.05	W/m×K	728.43	Calculated Property
λgas	0.06	W/m×K	818.96	Calculated Property
λgas	0.07	W/m×K	909.48	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.09]	W/m×K	[185.30; 473.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			8.12040e-02
Coefficient B			2.45710e+02
Coefficient C			-5.59460e+00
Coefficient D			1.32200e-02
Coefficient E			-2.50600e-05
Temperature range, min.			185.30
Temperature range, max.			473.15
λliquid	0.15	W/m×K	185.30	Calculated Property
λliquid	0.14	W/m×K	217.28	Calculated Property
λliquid	0.14	W/m×K	249.27	Calculated Property
λliquid	0.13	W/m×K	281.25	Calculated Property
λliquid	0.13	W/m×K	313.23	Calculated Property
λliquid	0.12	W/m×K	345.22	Calculated Property
λliquid	0.11	W/m×K	377.20	Calculated Property
λliquid	0.10	W/m×K	409.18	Calculated Property
λliquid	0.10	W/m×K	441.17	Calculated Property
λliquid	0.09	W/m×K	473.15	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, n-butyl-.

Mixtures

• Benzene, n-butyl- + 1-Propanone, 1-phenyl-
• Benzene, n-butyl- + Carbon dioxide
• Benzene, n-butyl- + Anisole
• Benzene, n-butyl- + Ethane, 1,1,2,2-tetrachloro-
• Benzene, n-butyl- + N-Formylmorpholine
• Benzene, n-butyl- + Acetic acid, butyl ester
• Benzene, n-butyl- + Water
• Benzene, n-butyl- + BUTYLCYCLOHEXANE + Nonane, 2,2,4,4,6,8,8-heptamethyl-
• Benzene, n-butyl- + Dodecane + BUTYLCYCLOHEXANE
• Benzene, n-butyl- + Dodecane + Nonane, 2,2,4,4,6,8,8-heptamethyl-
• Benzene, n-butyl- + Propanamide, N,N-bis(2-ethylhexyl)-2-methyl-
• Benzene, n-butyl- + Hexadecane + BUTYLCYCLOHEXANE
• Benzene, n-butyl- + Decane
• Benzene, n-butyl- + Dodecane
• Benzene, n-butyl- + Tetradecane
• Benzene, n-butyl- + Hexadecane
• Heptadecane + Benzene, n-butyl-
• Formic acid, propyl ester + Benzene, n-butyl-
• Benzene, n-butyl- + Benzene, chloro-
• Benzene, n-butyl- + Benzene, (chloromethyl)-

Find more mixtures with Benzene, n-butyl-.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons. J. Chem. Eng. Data 1995, 40, 547-558.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• 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)
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• 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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