Chemical Properties of Benzene, nitro- (CAS 98-95-3)

InChI

InChI=1S/C6H5NO2/c8-7(9)6-4-2-1-3-5-6/h1-5H

InChI Key

LQNUZADURLCDLV-UHFFFAOYSA-N

Formula

C6H5NO2

SMILES

O=[N+]([O-])c1ccccc1

Molecular Weight¹

123.11

CAS

98-95-3

Other Names

• Essence of Mirbane
• Essence of Myrbane
• Mirbane oil
• NCI-C60082
• NSC 9573
• Nitrobenzeen
• Nitrobenzen
• Nitrobenzene
• Nitrobenzol
• Oil of Mirbane
• Oil of Myrbane
• Rcra waste number U169
• UN 1662

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• α_p : Isobaric thermal expansion coefficient (1/K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• Δ_fG° : Standard Gibbs free energy of formation (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.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• 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°_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(P) : Boiling point at given pressure (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_fus(P) : Melting 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.
• 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	[0.3940; 0.4492]
ω	0.3940		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4492		ChemSep v8.3 pure component data Compiled value
PAff	800.30	kJ/mol	NIST
BasG	769.50	kJ/mol	NIST
ΔcH°liquid	[-3096.00; -3073.80]	kJ/mol
ΔcH°liquid	-3088.08 ± 0.42	kJ/mol	NIST
ΔcH°liquid	-3096.00	kJ/mol	NIST
ΔcH°liquid	-3073.80	kJ/mol	NIST
μ	4.23	debye	ChemSep v8.3 pure component data Compiled value
η	0.0016860	Pa×s	Ion Pair and Triple Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of Carbon Tetrachloride + Nitrobenzene
EA	[0.40; 1.18]	eV
EA	1.00 ± 0.01	eV	NIST
EA	1.01 ± 0.10	eV	NIST
EA	1.00 ± 0.06	eV	NIST
EA	1.00 ± 0.02	eV	NIST
EA	1.02 ± 0.05	eV	NIST
EA	1.18 ± 0.05	eV	NIST
EA	1.10	eV	NIST
EA	0.70 ± 0.20	eV	NIST
EA	Outlier 0.40	eV	NIST
ΔfG°	163.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[67.50; 68.53]	kJ/mol
ΔfH°gas	67.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	68.53 ± 0.67	kJ/mol	NIST
ΔfH°liquid	[-16.00; 12.50]	kJ/mol
ΔfH°liquid	12.50 ± 0.54	kJ/mol	NIST
ΔfH°liquid	-16.00	kJ/mol	NIST
ΔfusH°	16.70	kJ/mol	Joback Calculated Property
ΔvapH°	[54.50; 56.10]	kJ/mol
ΔvapH°	54.50	kJ/mol	NIST
ΔvapH°	55.01 ± 0.02	kJ/mol	NIST
ΔvapH°	55.00	kJ/mol	NIST
ΔvapH°	56.10 ± 1.70	kJ/mol	NIST
ΔvapH°	56.10 ± 1.70	kJ/mol	NIST
IE	[9.60; 10.80]	eV
IE	9.94 ± 0.08	eV	NIST
IE	9.67	eV	NIST
IE	9.80	eV	NIST
IE	10.16 ± 0.08	eV	NIST
IE	9.92	eV	NIST
IE	10.16 ± 0.08	eV	NIST
IE	9.87 ± 0.05	eV	NIST
IE	9.93	eV	NIST
IE	9.60	eV	NIST
IE	9.99	eV	NIST
IE	9.99 ± 0.01	eV	NIST
IE	9.85 ± 0.03	eV	NIST
IE	9.94 ± 0.03	eV	NIST
IE	9.90	eV	NIST
IE	9.86 ± 0.05	eV	NIST
IE	9.90 ± 0.03	eV	NIST
IE	10.16 ± 0.04	eV	NIST
IE	9.70 ± 0.10	eV	NIST
IE	9.92	eV	NIST
IE	9.86	eV	NIST
IE	9.90	eV	NIST
IE	9.92	eV	NIST
IE	9.93	eV	NIST
IE	Outlier 10.80	eV	NIST
IE	9.93	eV	NIST
IE	10.10 ± 0.10	eV	NIST
IE	9.88 ± 0.01	eV	NIST
IE	10.26	eV	NIST
log10WS	[-1.81; -1.80]
log10WS	-1.81		Aq. Solubility Prediction
log10WS	-1.80		Estimated Solubility
logPoct/wat	1.595		Crippen Calculated Property
McVol	89.060	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
NFPA Health	3		KDB
NFPA Safety	2		KDB
Pc	[3495.71; 4400.00]	kPa
Pc	3495.71	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4400.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	6.70e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[180.05; 1114.00]
Inp	1049.40		NIST
Inp	1058.30		NIST
Inp	1066.70		NIST
Inp	1049.20		NIST
Inp	1057.40		NIST
Inp	1068.50		NIST
Inp	1048.20		NIST
Inp	1054.00		NIST
Inp	1103.00		NIST
Inp	1103.00		NIST
Inp	1085.00		NIST
Inp	1075.00		NIST
Inp	1075.00		NIST
Inp	1076.00		NIST
Inp	1114.00		NIST
Inp	1071.00		NIST
Inp	1088.00		NIST
Inp	1100.00		NIST
Inp	1100.00		NIST
Inp	1088.80		NIST
Inp	1076.00		NIST
Inp	1081.00		NIST
Inp	1059.00		NIST
Inp	1046.00		NIST
Inp	1052.00		NIST
Inp	1056.00		NIST
Inp	1066.00		NIST
Inp	1076.00		NIST
Inp	1047.00		NIST
Inp	1059.00		NIST
Inp	1062.00		NIST
Inp	1084.00		NIST
Inp	1062.00		NIST
Inp	1068.00		NIST
Inp	1062.00		NIST
Inp	1046.00		NIST
Inp	1057.00		NIST
Inp	1046.00		NIST
Inp	1046.00		NIST
Inp	Outlier 180.05		NIST
Inp	1076.00		NIST
Inp	1056.00		NIST
Inp	1088.80		NIST
Inp	1049.40		NIST
Inp	1068.50		NIST
Inp	1085.00		NIST
Inp	1071.00		NIST
Inp	1100.00		NIST
Ip	[1683.00; 1683.00]
Ip	1683.00		NIST
Ip	1683.00		NIST
Ip	1683.00		NIST
S°liquid	224.30	J/mol×K	NIST
Tboil	[478.15; 485.09]	K
Tboil	483.95	K	ChemSep v8.3 pure component data Compiled value
Tboil	483.90	K	KDB
Tboil	483.80 ± 0.40	K	NIST
Tboil	484.00 ± 1.00	K	NIST
Tboil	484.20 ± 0.50	K	NIST
Tboil	483.70 ± 0.50	K	NIST
Tboil	484.00	K	NIST
Tboil	483.70 ± 0.50	K	NIST
Tboil	483.55 ± 0.40	K	NIST
Tboil	483.71 ± 0.40	K	NIST
Tboil	483.95 ± 0.70	K	NIST
Tboil	481.10 ± 1.00	K	NIST
Tboil	483.95 ± 0.50	K	NIST
Tboil	485.09 ± 0.25	K	NIST
Tboil	482.15 ± 1.00	K	NIST
Tboil	483.90 ± 0.50	K	NIST
Tboil	483.90 ± 0.30	K	NIST
Tboil	483.95 ± 0.30	K	NIST
Tboil	483.90 ± 0.30	K	NIST
Tboil	483.90 ± 0.50	K	NIST
Tboil	482.65 ± 0.50	K	NIST
Tboil	484.00 ± 0.40	K	NIST
Tboil	482.15 ± 2.00	K	NIST
Tboil	482.00 ± 2.00	K	NIST
Tboil	484.00 ± 0.35	K	NIST
Tboil	483.95 ± 1.00	K	NIST
Tboil	Outlier 478.15 ± 1.50	K	NIST
Tc	[712.00; 719.00]	K
Tc	712.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	719.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[278.80; 279.15]	K
Tfus	279.00	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	278.91	K	ChemSep v8.3 pure component data Compiled value
Tfus	278.81	K	KDB
Tfus	278.82	K	Aq. Solubility Prediction
Tfus	278.90 ± 0.20	K	NIST
Tfus	Outlier 279.15 ± 1.00	K	NIST
Tfus	278.90 ± 0.20	K	NIST
Tfus	278.87 ± 0.15	K	NIST
Tfus	278.89 ± 0.10	K	NIST
Tfus	Outlier 279.15 ± 0.50	K	NIST
Tfus	278.85 ± 0.50	K	NIST
Tfus	278.84 ± 0.07	K	NIST
Tfus	278.80 ± 0.08	K	NIST
Tfus	278.80 ± 0.08	K	NIST
Tfus	278.85 ± 0.20	K	NIST
Tfus	279.00 ± 1.50	K	NIST
Tfus	278.90 ± 0.30	K	NIST
Tfus	279.00 ± 1.50	K	NIST
Tfus	278.85 ± 0.20	K	NIST
Tfus	278.90 ± 0.30	K	NIST
Ttriple	278.87	K	ChemSep v8.3 pure component data Compiled value
UQi	3.14		ChemSep v8.3 pure component data Compiled value
URi	4.13		ChemSep v8.3 pure component data Compiled value
Vc	[0.340; 0.349]	m3/kmol
Vc	0.340	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.349	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2570000		ChemSep v8.3 pure component data Compiled value
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[176.00; 188.70]	J/mol×K	[293.00; 335.50]
Cp,liquid	180.20	J/mol×K	293.00	NIST
Cp,liquid	179.90	J/mol×K	293.00	NIST
Cp,liquid	179.95	J/mol×K	293.15	NIST
Cp,liquid	186.73	J/mol×K	298.00	NIST
Cp,liquid	177.80	J/mol×K	298.00	NIST
Cp,liquid	186.69	J/mol×K	298.10	NIST
Cp,liquid	181.13	J/mol×K	298.15	NIST
Cp,liquid	176.00	J/mol×K	303.00	NIST
Cp,liquid	177.40	J/mol×K	303.00	NIST
Cp,liquid	177.30	J/mol×K	303.15	NIST
Cp,liquid	188.70	J/mol×K	335.50	NIST
η	[0.0015286; 0.0019834]	Pa×s	[293.15; 308.15]
η	0.0019834	Pa×s	293.15	Densities and Viscosities of Binary and Ternary Mixtures of (Nitrobenzene + 1-Bromobutane), (1-Bromobutane + Methylcyclohexane), (Nitrobenzene + Methylcyclohexane), and (Methylcyclohexane + Nitrobenzene + 1-Bromobutane) from (293.15 to 308.15) K
η	0.0017910	Pa×s	298.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0016860	Pa×s	298.15	Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
η	0.0018095	Pa×s	298.15	Densities and Viscosities of Binary and Ternary Mixtures of (Nitrobenzene + 1-Bromobutane), (1-Bromobutane + Methylcyclohexane), (Nitrobenzene + Methylcyclohexane), and (Methylcyclohexane + Nitrobenzene + 1-Bromobutane) from (293.15 to 308.15) K
η	0.0016187	Pa×s	303.15	Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
η	0.0016595	Pa×s	303.15	Densities and Viscosities of Binary and Ternary Mixtures of (Nitrobenzene + 1-Bromobutane), (1-Bromobutane + Methylcyclohexane), (Nitrobenzene + Methylcyclohexane), and (Methylcyclohexane + Nitrobenzene + 1-Bromobutane) from (293.15 to 308.15) K
η	0.0015430	Pa×s	308.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0015543	Pa×s	308.15	Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
η	0.0015286	Pa×s	308.15	Densities and Viscosities of Binary and Ternary Mixtures of (Nitrobenzene + 1-Bromobutane), (1-Bromobutane + Methylcyclohexane), (Nitrobenzene + Methylcyclohexane), and (Methylcyclohexane + Nitrobenzene + 1-Bromobutane) from (293.15 to 308.15) K
ΔfusH	[10.81; 12.12]	kJ/mol	[278.80; 278.90]
ΔfusH	12.12	kJ/mol	278.80	NIST
ΔfusH	12.12	kJ/mol	278.80	NIST
ΔfusH	12.12	kJ/mol	278.80	NIST
ΔfusH	10.81	kJ/mol	278.90	NIST
ΔvapH	[48.50; 56.10]	kJ/mol	[287.50; 445.00]
ΔvapH	54.70	kJ/mol	287.50	NIST
ΔvapH	56.10 ± 0.42	kJ/mol	291.00	NIST
ΔvapH	56.10 ± 0.42	kJ/mol	291.00	NIST
ΔvapH	52.50	kJ/mol	293.00	NIST
ΔvapH	54.30	kJ/mol	303.00	NIST
ΔvapH	48.90	kJ/mol	425.00	NIST
ΔvapH	48.50	kJ/mol	445.00	NIST
Pvap	[95.30; 95.50]	kPa	[481.45; 483.05]
Pvap	95.50	kPa	481.45	Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
Pvap	95.30	kPa	483.05	Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
n0	[1.54005; 1.55488]		[293.15; 318.15]
n0	1.55488		293.15	A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
n0	1.54900		293.15	Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
n0	1.55000		298.15	Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
n0	1.55000		298.15	Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0	1.54930		298.15	Physico-chemical studies of sodium tetraphenylborate and tetrabutylammonium tetraphenylborate in pure nitrobenzene and nitromethane and their binaries probed by conductometry, refractometry and FT-IR spectroscopy
n0	1.54992		298.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.55000		298.15	Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
n0	1.54746		303.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.54760		303.15	Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
n0	1.54500		308.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.54250		313.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.54005		318.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
ρl	[1163.32; 1212.99]	kg/m3	[283.15; 333.15]
ρl	1212.99	kg/m3	283.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	1208.01	kg/m3	288.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	1211.53	kg/m3	288.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1202.61	kg/m3	293.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1203.05	kg/m3	293.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	1198.80	kg/m3	293.15	Isobaric Vapor Liquid Equilibrium Data of Acrylonitrile (1) + Heptan-1-ol (2), Acrylonitrile (1) + Ethanol (2), and Nitrobenzene (1) + Heptan-1-ol (2) at 96.5 kPa
ρl	1203.05	kg/m3	293.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1198.00	kg/m3	298.15	Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
ρl	1198.12	kg/m3	298.15	A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
ρl	1198.20	kg/m3	298.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	1198.36	kg/m3	298.15	Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
ρl	1198.00	kg/m3	298.15	Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
ρl	1198.91	kg/m3	298.15	Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
ρl	1198.20	kg/m3	298.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	1198.01	kg/m3	298.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1193.25	kg/m3	303.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	1189.60	kg/m3	303.15	Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
ρl	1193.40	kg/m3	303.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
ρl	1193.45	kg/m3	303.15	Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	1193.15	kg/m3	303.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1193.50	kg/m3	303.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1193.25	kg/m3	303.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	1188.17	kg/m3	308.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	1188.29	kg/m3	308.15	Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	1189.40	kg/m3	308.15	Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
ρl	1183.21	kg/m3	313.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1183.69	kg/m3	313.15	Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	1183.21	kg/m3	313.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	1187.20	kg/m3	313.15	Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
ρl	1178.24	kg/m3	318.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	1177.32	kg/m3	318.15	Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	1173.26	kg/m3	323.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	1173.27	kg/m3	323.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1163.32	kg/m3	333.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ΔfusS	[38.80; 43.48]	J/mol×K	[278.80; 278.90]
ΔfusS	43.48	J/mol×K	278.80	NIST
ΔfusS	38.80	J/mol×K	278.90	NIST
γ	[0.04; 0.04]	N/m	[303.15; 323.15]
γ	0.04	N/m	303.15	Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
γ	0.04	N/m	313.15	Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
γ	0.04	N/m	323.15	Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	483.05	K	95.30	Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
Tfus(P)	[299.74; 614.38]	K	[100000.00; 3000000.00]
Tfus(P)	299.74	K	100000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	320.77	K	200000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	340.02	K	300000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	360.41	K	400000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	378.61	K	500000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	395.90	K	600000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	412.30	K	700000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	427.24	K	800000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	442.98	K	900000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	462.61	K	1000000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	516.38	K	1500000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	565.62	K	2000000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	595.88	K	2500000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	614.38	K	3000000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Speed of sound, m/s (1)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
288.15	5000.00	0.0008
288.15	10000.00	0.0008
288.15	15000.00	0.0008
288.15	20000.00	0.0008
288.15	25000.00	0.0008
288.15	30000.00	0.0008
288.15	35000.00	0.0007
288.15	40000.00	0.0007
288.15	45000.00	0.0007
288.15	50000.00	0.0007
288.15	55000.00	0.0007
298.15	5000.00	0.0008
298.15	10000.00	0.0008
298.15	15000.00	0.0008
298.15	20000.00	0.0008
298.15	25000.00	0.0008
298.15	30000.00	0.0008
298.15	35000.00	0.0008
298.15	40000.00	0.0007
298.15	45000.00	0.0007
298.15	50000.00	0.0007
298.15	55000.00	0.0007
308.15	5000.00	0.0008
308.15	10000.00	0.0008
308.15	15000.00	0.0008
308.15	20000.00	0.0008
308.15	25000.00	0.0008
308.15	30000.00	0.0008
308.15	35000.00	0.0008
308.15	40000.00	0.0007
308.15	45000.00	0.0007
308.15	50000.00	0.0007
308.15	55000.00	0.0007
318.15	5000.00	0.0008
318.15	10000.00	0.0008
318.15	15000.00	0.0008
318.15	20000.00	0.0008
318.15	25000.00	0.0008
318.15	30000.00	0.0008
318.15	35000.00	0.0007
318.15	40000.00	0.0007
318.15	45000.00	0.0007
318.15	50000.00	0.0007
318.15	55000.00	0.0007
328.15	5000.00	0.0008
328.15	10000.00	0.0008
328.15	15000.00	0.0008
328.15	20000.00	0.0008
328.15	25000.00	0.0008
328.15	30000.00	0.0008
328.15	35000.00	0.0008
328.15	40000.00	0.0007
328.15	45000.00	0.0007
328.15	50000.00	0.0007
328.15	55000.00	0.0007
338.15	5000.00	0.0008
338.15	10000.00	0.0008
338.15	15000.00	0.0008
338.15	20000.00	0.0008
338.15	25000.00	0.0008
338.15	30000.00	0.0008
338.15	35000.00	0.0008
338.15	40000.00	0.0007
338.15	45000.00	0.0007
338.15	50000.00	0.0007
338.15	55000.00	0.0007
348.15	5000.00	0.0009
348.15	10000.00	0.0008
348.15	15000.00	0.0008
348.15	20000.00	0.0008
348.15	25000.00	0.0008
348.15	30000.00	0.0008
348.15	35000.00	0.0008
348.15	40000.00	0.0007
348.15	45000.00	0.0007
348.15	50000.00	0.0007
348.15	55000.00	0.0007
Reference

Speed of sound, m/s

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Frequency, MHz - Liquid	Speed of sound, m/s - Liquid
303.15	100.00	2.0	1445.6
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[124.54; 288.80]	J/mol×K	[263.15; 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			1.12710e+02
Coefficient B			-1.11430e+03
Coefficient C			7.02224e+00
Coefficient D			-1.30440e-03
Coefficient E			3.76990e-07
Temperature range, min.			263.15
Temperature range, max.			1500.00
Cp,gas	124.54	J/mol×K	263.15	Calculated Property
Cp,gas	156.46	J/mol×K	400.58	Calculated Property
Cp,gas	190.84	J/mol×K	538.01	Calculated Property
Cp,gas	218.71	J/mol×K	675.43	Calculated Property
Cp,gas	239.21	J/mol×K	812.86	Calculated Property
Cp,gas	253.96	J/mol×K	950.29	Calculated Property
Cp,gas	264.88	J/mol×K	1087.72	Calculated Property
Cp,gas	273.56	J/mol×K	1225.14	Calculated Property
Cp,gas	281.23	J/mol×K	1362.57	Calculated Property
Cp,gas	288.80	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[180.71; 264.22]	J/mol×K	[278.87; 483.95]	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			1.46460e+02
Coefficient B			1.16060e+03
Coefficient C			-6.46641e+00
Coefficient D			2.45750e-02
Coefficient E			-1.30490e-05
Temperature range, min.			278.87
Temperature range, max.			483.95
Cp,liquid	180.71	J/mol×K	278.87	Calculated Property
Cp,liquid	183.31	J/mol×K	301.66	Calculated Property
Cp,liquid	187.33	J/mol×K	324.44	Calculated Property
Cp,liquid	192.80	J/mol×K	347.23	Calculated Property
Cp,liquid	199.81	J/mol×K	370.02	Calculated Property
Cp,liquid	208.51	J/mol×K	392.80	Calculated Property
Cp,liquid	219.11	J/mol×K	415.59	Calculated Property
Cp,liquid	231.79	J/mol×K	438.38	Calculated Property
Cp,liquid	246.76	J/mol×K	461.16	Calculated Property
Cp,liquid	264.22	J/mol×K	483.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0031127; 0.0001856]	Pa×s	[273.15; 600.00]	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			-7.86520e+01
Coefficient B			4.20200e+03
Coefficient C			1.03700e+01
Coefficient D			-9.10950e-06
Coefficient E			2.00000e+00
Temperature range, min.			273.15
Temperature range, max.			600.00
η	0.0031127	Pa×s	273.15	Calculated Property
η	0.0015402	Pa×s	309.47	Calculated Property
η	0.0009415	Pa×s	345.78	Calculated Property
η	0.0006568	Pa×s	382.10	Calculated Property
η	0.0004975	Pa×s	418.42	Calculated Property
η	0.0003962	Pa×s	454.73	Calculated Property
η	0.0003245	Pa×s	491.05	Calculated Property
η	0.0002693	Pa×s	527.37	Calculated Property
η	0.0002241	Pa×s	563.68	Calculated Property
η	0.0001856	Pa×s	600.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[57.07; 18.23]	kJ/mol	[278.91; 695.84]	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			4.98840e+01
Coefficient B			-2.08130e+00
Coefficient C			7.52150e+00
Coefficient D			-8.81260e+00
Coefficient E			3.69470e+00
Critical temperature, Tc (K)			7.19000e+02
Temperature range, min.			278.91
Temperature range, max.			695.84
ΔvapH	57.07	kJ/mol	278.91	Calculated Property
ΔvapH	54.28	kJ/mol	325.24	Calculated Property
ΔvapH	51.28	kJ/mol	371.56	Calculated Property
ΔvapH	48.23	kJ/mol	417.89	Calculated Property
ΔvapH	45.17	kJ/mol	464.21	Calculated Property
ΔvapH	42.00	kJ/mol	510.54	Calculated Property
ΔvapH	38.47	kJ/mol	556.86	Calculated Property
ΔvapH	34.13	kJ/mol	603.19	Calculated Property
ΔvapH	28.11	kJ/mol	649.51	Calculated Property
ΔvapH	18.23	kJ/mol	695.84	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[359.28; 513.96]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.53379e+01
Coefficient B			-4.64614e+03
Coefficient C			-5.05750e+01
Temperature range, min.			359.28
Temperature range, max.			513.96
Pvap	1.33	kPa	359.28	Calculated Property
Pvap	2.95	kPa	376.47	Calculated Property
Pvap	6.02	kPa	393.65	Calculated Property
Pvap	11.49	kPa	410.84	Calculated Property
Pvap	20.67	kPa	428.03	Calculated Property
Pvap	35.33	kPa	445.21	Calculated Property
Pvap	57.75	kPa	462.40	Calculated Property
Pvap	90.75	kPa	479.59	Calculated Property
Pvap	137.72	kPa	496.77	Calculated Property
Pvap	202.63	kPa	513.96	Calculated Property
Pvap	[1.39e-03; 3233.25]	kPa	[263.15; 719.00]	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			1.05322e+02
Coefficient B			-1.05389e+04
Coefficient C			-1.29569e+01
Coefficient D			5.11636e-06
Coefficient E			2.00000e+00
Temperature range, min.			263.15
Temperature range, max.			719.00
Pvap	1.39e-03	kPa	263.15	Calculated Property
Pvap	0.11	kPa	313.80	Calculated Property
Pvap	1.94	kPa	364.45	Calculated Property
Pvap	14.95	kPa	415.10	Calculated Property
Pvap	66.82	kPa	465.75	Calculated Property
Pvap	208.18	kPa	516.40	Calculated Property
Pvap	507.65	kPa	567.05	Calculated Property
Pvap	1045.50	kPa	617.70	Calculated Property
Pvap	1914.85	kPa	668.35	Calculated Property
Pvap	3233.25	kPa	719.00	Calculated Property
Pvap	[6.43e-03; 4167.87]	kPa	[278.91; 719.00]	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			1.29288e+02
Coefficient B			-1.14658e+04
Coefficient C			-1.66824e+01
Coefficient D			9.14721e-06
Coefficient E			0.00000e+00
Temperature range, min.			278.91
Temperature range, max.			719.00
Pvap	6.43e-03	kPa	278.91	Calculated Property
Pvap	0.26	kPa	327.81	Calculated Property
Pvap	3.31	kPa	376.71	Calculated Property
Pvap	20.44	kPa	425.61	Calculated Property
Pvap	80.01	kPa	474.51	Calculated Property
Pvap	232.70	kPa	523.40	Calculated Property
Pvap	556.46	kPa	572.30	Calculated Property
Pvap	1169.96	kPa	621.20	Calculated Property
Pvap	2264.56	kPa	670.10	Calculated Property
Pvap	4167.87	kPa	719.00	Calculated Property
Pvap	[10.99; 101.25]	kPa	[407.30; 483.78]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43118e+01
Coefficient B			-3.97793e+03
Coefficient C			-7.34380e+01
Reference			Brown, 1952
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			407.30
Temperature range, max.			483.78
Pvap	10.99	kPa	407.30	Calculated Property
Pvap	14.77	kPa	415.80	Calculated Property
Pvap	19.57	kPa	424.30	Calculated Property
Pvap	25.59	kPa	432.79	Calculated Property
Pvap	33.05	kPa	441.29	Calculated Property
Pvap	42.18	kPa	449.79	Calculated Property
Pvap	53.27	kPa	458.29	Calculated Property
Pvap	66.60	kPa	466.78	Calculated Property
Pvap	82.48	kPa	475.28	Calculated Property
Pvap	101.25	kPa	483.78	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1222.72; 352.75]	kg/m3	[273.15; 719.00]	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			8.50981e+01
Coefficient B			2.41240e-01
Coefficient C			7.19000e+02
Coefficient D			2.81370e-01
Temperature range, min.			273.15
Temperature range, max.			719.00
ρl	1222.72	kg/m3	273.15	Calculated Property
ρl	1174.16	kg/m3	322.69	Calculated Property
ρl	1123.23	kg/m3	372.23	Calculated Property
ρl	1069.35	kg/m3	421.77	Calculated Property
ρl	1011.66	kg/m3	471.31	Calculated Property
ρl	948.83	kg/m3	520.84	Calculated Property
ρl	878.57	kg/m3	570.38	Calculated Property
ρl	796.24	kg/m3	619.92	Calculated Property
ρl	689.28	kg/m3	669.46	Calculated Property
ρl	352.75	kg/m3	719.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.02]	N/m	[278.95; 483.95]	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			8.09883e-02
Coefficient B			-1.18500e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			278.95
Temperature range, max.			483.95
γ	0.05	N/m	278.95	Calculated Property
γ	0.05	N/m	301.73	Calculated Property
γ	0.04	N/m	324.51	Calculated Property
γ	0.04	N/m	347.28	Calculated Property
γ	0.04	N/m	370.06	Calculated Property
γ	0.03	N/m	392.84	Calculated Property
γ	0.03	N/m	415.62	Calculated Property
γ	0.03	N/m	438.39	Calculated Property
γ	0.03	N/m	461.17	Calculated Property
γ	0.02	N/m	483.95	Calculated Property
γ	[0.05; 2.30e-05]	N/m	[273.15; 716.77]	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			-1.87080e-02
Coefficient B			9.85920e+01
Coefficient C			-3.18390e+00
Coefficient D			1.34010e-03
Coefficient E			-3.68220e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 719 K.
Temperature range, min.			273.15
Temperature range, max.			716.77
γ	0.05	N/m	273.15	Calculated Property
γ	0.04	N/m	322.44	Calculated Property
γ	0.03	N/m	371.73	Calculated Property
γ	0.03	N/m	421.02	Calculated Property
γ	0.02	N/m	470.31	Calculated Property
γ	0.02	N/m	519.61	Calculated Property
γ	0.01	N/m	568.90	Calculated Property
γ	0.01	N/m	618.19	Calculated Property
γ	0.00	N/m	667.48	Calculated Property
γ	2.30e-05	N/m	716.77	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.06]	W/m×K	[278.87; 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			1.43730e-04
Coefficient B			9.61500e-01
Coefficient C			7.18000e+02
Coefficient D			-2.78520e-03
Temperature range, min.			278.87
Temperature range, max.			1000.00
λgas	0.01	W/m×K	278.87	Calculated Property
λgas	0.01	W/m×K	359.00	Calculated Property
λgas	0.02	W/m×K	439.12	Calculated Property
λgas	0.02	W/m×K	519.25	Calculated Property
λgas	0.03	W/m×K	599.37	Calculated Property
λgas	0.04	W/m×K	679.50	Calculated Property
λgas	0.04	W/m×K	759.62	Calculated Property
λgas	0.05	W/m×K	839.75	Calculated Property
λgas	0.06	W/m×K	919.87	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.14]	W/m×K	[273.15; 400.00]	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			1.12930e-01
Coefficient B			-4.01920e+02
Coefficient C			1.28260e+00
Coefficient D			-1.32070e-02
Coefficient E			7.59320e-06
Temperature range, min.			273.15
Temperature range, max.			400.00
λliquid	0.15	W/m×K	273.15	Calculated Property
λliquid	0.15	W/m×K	287.24	Calculated Property
λliquid	0.15	W/m×K	301.34	Calculated Property
λliquid	0.15	W/m×K	315.43	Calculated Property
λliquid	0.14	W/m×K	329.53	Calculated Property
λliquid	0.14	W/m×K	343.62	Calculated Property
λliquid	0.14	W/m×K	357.72	Calculated Property
λliquid	0.14	W/m×K	371.81	Calculated Property
λliquid	0.14	W/m×K	385.91	Calculated Property
λliquid	0.14	W/m×K	400.00	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, nitro-.

Mixtures

• Benzene, nitro- + Benzene
• Benzene, nitro- + Toluene
• Benzene, nitro- + Benzene, ethyl-
• Benzene, nitro- + Styrene
• Benzene, nitro- + o-Xylene
• Benzene, nitro- + Benzene, 1,3-dimethyl-
• Benzene, nitro- + p-Xylene
• Benzene, nitro- + TETRABUTYLAMMONIUM HEXAFLUOROPHOSPHATE
• Benzene, nitro- + Bis(2-ethylhexyl)hydrogen phosphate
• Benzene, nitro- + 1-Hexanol
• Benzene, nitro- + Methyl Alcohol
• Benzene, nitro- + Ethanol
• Benzene, nitro- + 1-Propanol
• Benzene, nitro- + 2-Propanol
• Benzene, nitro- + 1-Butanol
• Benzene, nitro- + 1-Propanol, 2-methyl-
• 2-Propanol, 2-methyl- + Benzene, nitro-
• Benzene, nitro- + Triethylamine
• Benzene, nitro- + 2,4,6-trimethyl-2,4,6-tris(3,3,3-trifluoropropyl)-1,3,5,2,4,6-trioxatrisilinane
• Benzene, nitro- + Methane, nitro-

Find more mixtures with Benzene, nitro-.

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).
• 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).
• 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
• Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
• Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
• Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
• Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
• Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
• Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
• Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
• Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
• Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
• The liquid-liquid coexistence curves of {x nitrobenzene + (1 - x) 2-methylpentane} and {x nitrobenzene + (1 - x) isooctane} in the critical region
• Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
• A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
• Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
• Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
• Studies on intermolecular interactions in nitrobenzene + alkoxyethanol binary mixtures by relative permittivity measurements at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
• Physico-chemical studies of sodium tetraphenylborate and tetrabutylammonium tetraphenylborate in pure nitrobenzene and nitromethane and their binaries probed by conductometry, refractometry and FT-IR spectroscopy
• Enthalpies of formation of nitromethane and nitrobenzene: New experiments vs. quantum chemical calculations
• The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
• A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
• Ultrasonic and 31P NMR investigations of an acidic nuclear extractant with some monosubstituted benzenes
• The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
• Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
• Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
• Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
• Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
• Solvation of benzene and its simple mono derivatives in water-tertiary butanol mixtures
• Volumetric and electromagnetic properties of binary mixtures consist of benzene derivatives at different temperature and ternary mixtures with 1,2-dichloroethane at T = 293.15 K with application of the Prigogine-Flory-Patterson theory and PC-SAFT
• Enthalpies of solution and enthalpies of solvation of chloro- and nitro-substituted benzenes in 1-butyl-3-methyl imidazolium based ionic liquids at 298.15 K: Additivity of group contributions
• Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
• Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
• Temperature Dependences of Limiting Activity Coefficients and Henry s Law Constants for Nitrobenzene, Aniline, and Cyclohexylamine in Water
• Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
• Densities and Viscosities of Binary and Ternary Mixtures of (Nitrobenzene + 1-Bromobutane), (1-Bromobutane + Methylcyclohexane), (Nitrobenzene + Methylcyclohexane), and (Methylcyclohexane + Nitrobenzene + 1-Bromobutane) from (293.15 to 308.15) K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Isobaric Vapor Liquid Equilibrium Data of Acrylonitrile (1) + Heptan-1-ol (2), Acrylonitrile (1) + Ethanol (2), and Nitrobenzene (1) + Heptan-1-ol (2) at 96.5 kPa
• Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
• Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
• Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
• Assessing the Salting-Out Behavior of Nitrobenzene, 2-Nitrotoluene, and 3-Nitrotoluene from Solubility Values in Pure Water and Seawater at Temperatures between (277 and 314) K
• Liquid-Liquid Equilibria of Nitrobenzene-Inorganic Acid Systems at 298.15 K
• Ion Pair and Triple Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of Carbon Tetrachloride + Nitrobenzene
• Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
• Isobaric Thermal Expansivity of Highly Polar Nitrogen Compounds at Temperatures from (278.15 to 348.15) K and at Pressures from (5 to 55) MPa
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.