Chemical Properties of Benzene, chloro- (CAS 108-90-7)

InChI

InChI=1S/C6H5Cl/c7-6-4-2-1-3-5-6/h1-5H

InChI Key

MVPPADPHJFYWMZ-UHFFFAOYSA-N

Formula

C6H5Cl

SMILES

Clc1ccccc1

Molecular Weight¹

112.56

CAS

108-90-7

Other Names

• Abluton T30
• Benzene chloride
• CP 27
• Chloorbenzeen
• Chlorbenzene
• Chlorbenzol
• Chlorobenzen
• Chlorobenzene, mono-
• Chlorobenzenu
• Chlorobenzol
• Clorobenzene
• IP Carrier T 40
• MCB
• Monochloorbenzeen
• Monochlorbenzene
• Monochlorbenzol
• Monoclorobenzene
• NCI-C54886
• NSC 8433
• Tetrosin SP
• UN 1134
• chlorobenzene
• monochlorobenzene
• phenyl chloride

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_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°_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.

Physical Properties

Property	Value	Unit	Source
ω	[0.2490; 0.2510]
ω	0.2490		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2510		ChemSep v8.3 pure component data Compiled value
ω	0.2490		KDB
PAff	753.10	kJ/mol	NIST
Tig	913.15	K	KDB
BasG	724.60	kJ/mol	NIST
ΔcH°liquid	[-3112.70; -3108.90]	kJ/mol
ΔcH°liquid	-3112.70 ± 0.90	kJ/mol	NIST
ΔcH°liquid	-3110.70 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-3108.90 ± 0.79	kJ/mol	NIST
ΔcH°liquid	-3111.60 ± 8.40	kJ/mol	NIST
μ	[1.60; 1.69]	debye
μ	1.69	debye	ChemSep v8.3 pure component data Compiled value
μ	1.60	debye	KDB
LFL	1.30	% in Air	KDB
UFL	7.10	% in Air	KDB
Tflash,cc	309.26	K	KDB
Tflash,oc	302.04	K	KDB
ΔfG°	[98.29; 99.23]	kJ/mol
ΔfG°	98.29	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	99.23	kJ/mol	KDB
Rg	3.5680		KDB
ΔfH°gas	[51.09; 54.42]	kJ/mol
ΔfH°gas	52.22 ± 0.61	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	51.09	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	51.87	kJ/mol	KDB
ΔfH°gas	54.42	kJ/mol	NIST
ΔfH°liquid	[10.70; 11.50]	kJ/mol
ΔfH°liquid	11.50 ± 1.00	kJ/mol	NIST
ΔfH°liquid	10.70 ± 0.79	kJ/mol	NIST
ΔfusH°	9.53	kJ/mol	Joback Calculated Property
ΔvapH°	[36.60; 43.90]	kJ/mol
ΔvapH°	41.00	kJ/mol	NIST
ΔvapH°	40.30	kJ/mol	NIST
ΔvapH°	43.90	kJ/mol	NIST
ΔvapH°	41.00	kJ/mol	NIST
ΔvapH°	41.00 ± 0.10	kJ/mol	NIST
ΔvapH°	40.97 ± 0.06	kJ/mol	NIST
ΔvapH°	Outlier 36.60 ± 0.04	kJ/mol	NIST
IE	[8.80; 9.55]	eV
IE	9.07 ± 0.02	eV	NIST
IE	9.08	eV	NIST
IE	Outlier 8.80	eV	NIST
IE	9.07 ± 0.03	eV	NIST
IE	9.10	eV	NIST
IE	9.10 ± 0.02	eV	NIST
IE	9.10 ± 0.02	eV	NIST
IE	9.06 ± 0.01	eV	NIST
IE	9.09	eV	NIST
IE	Outlier 9.55	eV	NIST
IE	9.07 ± 0.02	eV	NIST
IE	9.10 ± 0.10	eV	NIST
IE	8.99	eV	NIST
IE	9.08 ± 0.01	eV	NIST
IE	9.04	eV	NIST
IE	9.05	eV	NIST
IE	9.07	eV	NIST
IE	9.07 ± 0.02	eV	NIST
IE	9.07	eV	NIST
IE	9.07	eV	NIST
IE	9.08	eV	NIST
IE	9.07	eV	NIST
IE	9.09	eV	NIST
log10WS	[-2.39; -2.38]
log10WS	-2.39		Aq. Solubility Prediction
log10WS	-2.38		Estimated Solubility
logPoct/wat	2.340		Crippen Calculated Property
McVol	83.880	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	[4519.10; 4530.00]	kPa
Pc	4530.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	4519.10	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4520.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4520.00	kPa	KDB
Pc	4519.10 ± 30.39	kPa	NIST
Ptriple	8.45e-03	kPa	ChemSep v8.3 pure component data Compiled value
ρc	364.68 ± 4.50	kg/m3	NIST
Inp	[811.00; 885.00]
Inp	859.30		NIST
Inp	859.00		NIST
Inp	853.80		NIST
Inp	Outlier 877.50		NIST
Inp	865.00		NIST
Inp	830.32		NIST
Inp	834.00		NIST
Inp	866.47		NIST
Inp	850.16		NIST
Inp	857.29		NIST
Inp	842.00		NIST
Inp	850.00		NIST
Inp	836.00		NIST
Inp	838.80		NIST
Inp	827.00		NIST
Inp	815.00		NIST
Inp	850.30		NIST
Inp	864.50		NIST
Inp	866.00		NIST
Inp	832.00		NIST
Inp	840.00		NIST
Inp	Outlier 880.00		NIST
Inp	Outlier 880.00		NIST
Inp	875.00		NIST
Inp	875.00		NIST
Inp	860.00		NIST
Inp	849.60		NIST
Inp	852.00		NIST
Inp	854.60		NIST
Inp	857.40		NIST
Inp	860.30		NIST
Inp	863.30		NIST
Inp	832.00		NIST
Inp	836.00		NIST
Inp	840.00		NIST
Inp	844.00		NIST
Inp	852.00		NIST
Inp	869.00		NIST
Inp	870.00		NIST
Inp	870.00		NIST
Inp	838.40		NIST
Inp	814.00		NIST
Inp	818.00		NIST
Inp	871.00		NIST
Inp	826.30		NIST
Inp	830.00		NIST
Inp	817.00		NIST
Inp	821.00		NIST
Inp	827.00		NIST
Inp	814.00		NIST
Inp	820.00		NIST
Inp	826.00		NIST
Inp	815.00		NIST
Inp	819.00		NIST
Inp	833.00		NIST
Inp	822.00		NIST
Inp	826.00		NIST
Inp	855.00		NIST
Inp	843.00		NIST
Inp	849.00		NIST
Inp	827.00		NIST
Inp	815.00		NIST
Inp	819.00		NIST
Inp	834.00		NIST
Inp	819.00		NIST
Inp	825.00		NIST
Inp	822.00		NIST
Inp	811.00		NIST
Inp	815.00		NIST
Inp	830.00		NIST
Inp	817.00		NIST
Inp	822.00		NIST
Inp	Outlier 885.00		NIST
Inp	833.00		NIST
Inp	Outlier 877.90		NIST
Inp	831.20		NIST
Inp	821.20		NIST
Inp	852.40		NIST
Inp	826.50		NIST
Inp	836.42		NIST
Inp	837.68		NIST
Inp	840.15		NIST
Inp	825.30		NIST
Inp	833.00		NIST
Inp	830.00		NIST
Inp	825.00		NIST
Inp	852.00		NIST
Inp	839.00		NIST
Inp	839.00		NIST
Inp	844.00		NIST
Inp	834.00		NIST
Inp	839.00		NIST
Inp	842.00		NIST
Inp	849.00		NIST
Inp	856.00		NIST
Inp	835.00		NIST
Inp	828.00		NIST
Inp	850.00		NIST
Inp	833.00		NIST
Inp	Outlier 880.00		NIST
Inp	850.00		NIST
Inp	844.00		NIST
Inp	837.00		NIST
Inp	835.00		NIST
Inp	864.00		NIST
Inp	841.00		NIST
Inp	842.00		NIST
Inp	846.00		NIST
Inp	850.00		NIST
Inp	834.00		NIST
Inp	839.00		NIST
Inp	850.00		NIST
Inp	852.00		NIST
Inp	850.00		NIST
Inp	839.00		NIST
Inp	855.00		NIST
Inp	844.00		NIST
Inp	839.00		NIST
Inp	Outlier 880.00		NIST
Inp	824.00		NIST
Inp	829.00		NIST
Inp	844.00		NIST
Inp	860.00		NIST
Inp	852.00		NIST
Inp	836.00		NIST
Inp	827.00		NIST
Inp	820.00		NIST
Inp	839.00		NIST
Inp	844.00		NIST
Inp	860.00		NIST
Inp	859.30		NIST
Inp	830.32		NIST
Inp	842.00		NIST
Inp	815.00		NIST
Inp	840.00		NIST
Inp	860.00		NIST
Inp	860.30		NIST
Inp	844.00		NIST
Inp	838.40		NIST
Inp	830.00		NIST
Inp	820.00		NIST
Inp	822.00		NIST
Inp	827.00		NIST
Inp	825.00		NIST
Inp	817.00		NIST
Inp	850.00		NIST
Inp	841.00		NIST
Inp	839.00		NIST
Inp	Outlier 877.90		NIST
Ip	[1188.00; 1279.10]
Ip	1257.10		NIST
Ip	1279.10		NIST
Ip	1224.00		NIST
Ip	1257.00		NIST
Ip	1231.00		NIST
Ip	1257.00		NIST
Ip	1270.00		NIST
Ip	1270.00		NIST
Ip	1219.00		NIST
Ip	1213.00		NIST
Ip	1243.90		NIST
Ip	1240.38		NIST
Ip	1226.05		NIST
Ip	1220.51		NIST
Ip	1241.00		NIST
Ip	1234.00		NIST
Ip	1202.00		NIST
Ip	1233.00		NIST
Ip	1238.00		NIST
Ip	1238.00		NIST
Ip	1209.00		NIST
Ip	Outlier 1188.00		NIST
Ip	1205.00		NIST
Ip	1241.00		NIST
Ip	1200.00		NIST
Ip	1238.00		NIST
Ip	1209.00		NIST
Ip	1257.10		NIST
Ip	1257.00		NIST
S°liquid	197.50	J/mol×K	NIST
Tboil	[402.15; 444.85]	K
Tboil	404.80	K	Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
Tboil	404.91	K	ChemSep v8.3 pure component data Compiled value
Tboil	404.87	K	KDB
Tboil	404.60 ± 0.40	K	NIST
Tboil	405.20 ± 0.50	K	NIST
Tboil	404.80 ± 0.50	K	NIST
Tboil	404.90 ± 0.50	K	NIST
Tboil	404.85 ± 0.40	K	NIST
Tboil	405.20	K	NIST
Tboil	404.95 ± 0.30	K	NIST
Tboil	404.15 ± 1.00	K	NIST
Tboil	404.90	K	NIST
Tboil	404.82 ± 0.40	K	NIST
Tboil	405.65 ± 0.40	K	NIST
Tboil	405.20 ± 0.60	K	NIST
Tboil	404.80 ± 0.70	K	NIST
Tboil	404.87 ± 0.25	K	NIST
Tboil	404.65 ± 0.30	K	NIST
Tboil	404.98 ± 0.25	K	NIST
Tboil	404.75 ± 0.30	K	NIST
Tboil	404.40 ± 0.40	K	NIST
Tboil	404.90 ± 0.40	K	NIST
Tboil	405.15 ± 1.50	K	NIST
Tboil	405.20 ± 0.40	K	NIST
Tboil	Outlier 444.85 ± 0.20	K	NIST
Tboil	404.70 ± 0.50	K	NIST
Tboil	404.90 ± 0.50	K	NIST
Tboil	404.95 ± 0.30	K	NIST
Tboil	404.20 ± 1.00	K	NIST
Tboil	405.11 ± 0.30	K	NIST
Tboil	405.15 ± 0.20	K	NIST
Tboil	405.00 ± 3.00	K	NIST
Tboil	404.60 ± 0.50	K	NIST
Tboil	404.70 ± 0.30	K	NIST
Tboil	404.45 ± 0.50	K	NIST
Tboil	404.82 ± 0.20	K	NIST
Tboil	404.90 ± 0.50	K	NIST
Tboil	405.15 ± 0.60	K	NIST
Tboil	404.90 ± 0.30	K	NIST
Tboil	404.90 ± 0.30	K	NIST
Tboil	404.80 ± 1.00	K	NIST
Tboil	404.98 ± 0.10	K	NIST
Tboil	405.15 ± 0.40	K	NIST
Tboil	404.83 ± 0.10	K	NIST
Tboil	405.20 ± 0.50	K	NIST
Tboil	405.20 ± 0.50	K	NIST
Tboil	404.85 ± 0.50	K	NIST
Tboil	405.15 ± 0.04	K	NIST
Tboil	405.12 ± 0.30	K	NIST
Tboil	404.15 ± 1.50	K	NIST
Tboil	405.15 ± 0.40	K	NIST
Tboil	405.15 ± 0.04	K	NIST
Tboil	405.15 ± 0.20	K	NIST
Tboil	405.15 ± 0.40	K	NIST
Tboil	405.15 ± 0.05	K	NIST
Tboil	404.65 ± 0.50	K	NIST
Tboil	402.15 ± 1.50	K	NIST
Tboil	405.50 ± 0.80	K	NIST
Tc	[632.35; 635.35]	K
Tc	633.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	632.40	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	632.40	K	ChemSep v8.3 pure component data Compiled value
Tc	632.40	K	KDB
Tc	632.35 ± 0.30	K	NIST
Tc	632.65 ± 6.00	K	NIST
Tc	Outlier 635.35 ± 2.00	K	NIST
Tfus	[227.57; 228.25]	K
Tfus	228.00	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	227.95	K	ChemSep v8.3 pure component data Compiled value
Tfus	227.90	K	KDB
Tfus	227.82	K	Aq. Solubility Prediction
Tfus	227.83 ± 0.06	K	NIST
Tfus	228.15 ± 1.00	K	NIST
Tfus	Outlier 227.57 ± 0.20	K	NIST
Tfus	228.00 ± 1.50	K	NIST
Tfus	228.15 ± 0.40	K	NIST
Tfus	227.95 ± 0.06	K	NIST
Tfus	227.95 ± 0.10	K	NIST
Tfus	227.92 ± 0.10	K	NIST
Tfus	227.80 ± 0.15	K	NIST
Tfus	228.05 ± 0.20	K	NIST
Tfus	227.95 ± 0.20	K	NIST
Tfus	227.95 ± 0.50	K	NIST
Tfus	Outlier 227.57 ± 0.10	K	NIST
Tfus	227.95 ± 0.50	K	NIST
Tfus	228.15 ± 0.30	K	NIST
Tfus	228.15 ± 0.30	K	NIST
Tfus	228.15 ± 0.25	K	NIST
Tfus	228.15 ± 2.00	K	NIST
Tfus	228.25 ± 0.50	K	NIST
Ttriple	[227.90; 227.96]	K
Ttriple	227.96	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	227.95	K	ChemSep v8.3 pure component data Compiled value
Ttriple	227.90 ± 0.20	K	NIST
Ttriple	227.90 ± 0.20	K	NIST
UQi	2.84		ChemSep v8.3 pure component data Compiled value
URi	3.79		ChemSep v8.3 pure component data Compiled value
Vc	[0.308; 0.308]	m3/kmol
Vc	0.308	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Vc	0.308	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.308	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.308	m3/kmol	KDB
Zc	[0.2647650; 0.2650000]
Zc	0.2650000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Zc	0.2650000		ChemSep v8.3 pure component data Compiled value
Zc	0.2647650		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[141.00; 164.34]	J/mol×K	[283.15; 353.15]
Cp,liquid	147.73	J/mol×K	283.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	148.14	J/mol×K	285.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	148.56	J/mol×K	287.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	148.99	J/mol×K	289.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	149.41	J/mol×K	291.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	149.85	J/mol×K	293.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	145.60	J/mol×K	293.20	NIST
Cp,liquid	150.29	J/mol×K	295.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	150.73	J/mol×K	297.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	141.00	J/mol×K	298.00	NIST
Cp,liquid	147.70	J/mol×K	298.00	NIST
Cp,liquid	150.08	J/mol×K	298.10	NIST
Cp,liquid	153.78	J/mol×K	298.15	NIST
Cp,liquid	152.10	J/mol×K	298.15	NIST
Cp,liquid	150.79	J/mol×K	298.15	NIST
Cp,liquid	151.18	J/mol×K	299.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	151.64	J/mol×K	301.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	150.60	J/mol×K	303.15	NIST
Cp,liquid	152.10	J/mol×K	303.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	152.56	J/mol×K	305.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	157.30	J/mol×K	305.60	NIST
Cp,liquid	153.03	J/mol×K	307.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	153.50	J/mol×K	309.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	153.97	J/mol×K	311.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	154.45	J/mol×K	313.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	154.93	J/mol×K	315.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	155.41	J/mol×K	317.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	155.90	J/mol×K	319.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	156.39	J/mol×K	321.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	156.88	J/mol×K	323.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	157.37	J/mol×K	325.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	157.86	J/mol×K	327.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	158.36	J/mol×K	329.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	158.86	J/mol×K	331.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	159.35	J/mol×K	333.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	159.85	J/mol×K	335.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	160.35	J/mol×K	337.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	160.85	J/mol×K	339.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	161.35	J/mol×K	341.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	161.85	J/mol×K	343.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	162.35	J/mol×K	345.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	162.85	J/mol×K	347.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	163.34	J/mol×K	349.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	163.84	J/mol×K	351.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	164.34	J/mol×K	353.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,solid	106.30	J/mol×K	216.80	NIST
η	[0.0004658; 0.0008432]	Pa×s	[293.00; 343.15]
η	0.0008432	Pa×s	293.00	Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
η	0.0008084	Pa×s	293.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0007570	Pa×s	298.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0007568	Pa×s	298.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0007560	Pa×s	298.15	Densities, Viscosities, and Thermodynamic Properties of (N,N-Dimethylformamide + Benzene + Chlorobenzene) Ternary Mixtures at (298.15, 303.15, 308.15, and 313.15) K
η	0.0007550	Pa×s	298.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0007422	Pa×s	298.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0007210	Pa×s	303.00	Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
η	0.0007258	Pa×s	303.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0007140	Pa×s	303.15	Densities, Viscosities, and Thermodynamic Properties of (N,N-Dimethylformamide + Benzene + Chlorobenzene) Ternary Mixtures at (298.15, 303.15, 308.15, and 313.15) K
η	0.0007140	Pa×s	303.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0007053	Pa×s	303.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0006770	Pa×s	308.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0006730	Pa×s	308.15	Densities, Viscosities, and Thermodynamic Properties of (N,N-Dimethylformamide + Benzene + Chlorobenzene) Ternary Mixtures at (298.15, 303.15, 308.15, and 313.15) K
η	0.0006790	Pa×s	308.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0006770	Pa×s	308.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0006247	Pa×s	313.00	Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
η	0.0006310	Pa×s	313.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0006350	Pa×s	313.15	Densities, Viscosities, and Thermodynamic Properties of (N,N-Dimethylformamide + Benzene + Chlorobenzene) Ternary Mixtures at (298.15, 303.15, 308.15, and 313.15) K
η	0.0006170	Pa×s	313.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0006240	Pa×s	313.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0005677	Pa×s	323.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0005069	Pa×s	333.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0004658	Pa×s	343.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
ΔfusH	[9.55; 9.56]	kJ/mol	[227.89; 227.90]
ΔfusH	9.56	kJ/mol	227.89	NIST
ΔfusH	9.56	kJ/mol	227.89	NIST
ΔfusH	9.55	kJ/mol	227.90	NIST
ΔfusH	9.55	kJ/mol	227.90	NIST
ΔvapH	[35.19; 48.10]	kJ/mol	[278.00; 501.00]
ΔvapH	37.30	kJ/mol	278.00	NIST
ΔvapH	48.10	kJ/mol	285.50	NIST
ΔvapH	38.80	kJ/mol	369.00	NIST
ΔvapH	35.19	kJ/mol	404.90	NIST
ΔvapH	36.55	kJ/mol	405.10	KDB
ΔvapH	35.40	kJ/mol	501.00	NIST
Pvap	[0.37; 101.33]	kPa	[274.50; 404.80]
Pvap	0.37	kPa	274.50	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	0.44	kPa	277.30	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	0.53	kPa	280.30	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	0.65	kPa	283.30	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	0.79	kPa	286.30	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	0.95	kPa	289.30	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	1.12	kPa	292.20	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	1.30	kPa	295.20	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	1.54	kPa	298.20	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	1.87	kPa	301.20	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	2.17	kPa	304.20	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	2.61	kPa	307.20	Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
Pvap	7.92	kPa	330.50	Vapor Pressure Measurements for 2-Chloromethylbenzoxazole and Vapor-Liquid Equilibrium Measurements for the Chlorobenzene + 2-Chloromethylbenzoxazole System
Pvap	10.59	kPa	337.40	Vapor Pressure Measurements for 2-Chloromethylbenzoxazole and Vapor-Liquid Equilibrium Measurements for the Chlorobenzene + 2-Chloromethylbenzoxazole System
Pvap	28.33	kPa	363.15	Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile
Pvap	95.30	kPa	402.35	Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
Pvap	95.50	kPa	402.85	Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
Pvap	101.33	kPa	404.80	Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
n0	[1.51072; 1.52480]		[293.15; 318.15]
n0	1.52480		293.15	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	1.52440		293.20	Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
n0	1.52176		298.15	Thermophysical properties of the binary mixtures of 2-methyl-tetrahydrofuran with benzene and halobenzenes
n0	1.52180		298.15	Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
n0	1.52190		298.15	(Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
n0	1.52176		298.15	Azeotropic behaviour of (benzene + cyclohexane + chlorobenzene) ternary mixture using chlorobenzene as entrainer at 101.3 kPa
n0	1.52180		298.15	Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0	1.52168		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	1.52230		298.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
n0	1.52180		298.15	Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
n0	1.51950		303.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
n0	1.51893		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	1.51600		303.15	Refractive properties, speed of sound and FT-IR study of binary mixtures of N-formylmorpholine with some halobenzenes at 303.15, 308.15 and 313.15 K
n0	1.51910		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	1.51629		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	1.51660		308.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
n0	1.51500		308.15	Refractive properties, speed of sound and FT-IR study of binary mixtures of N-formylmorpholine with some halobenzenes at 303.15, 308.15 and 313.15 K
n0	1.51348		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	1.51430		313.15	Refractive properties, speed of sound and FT-IR study of binary mixtures of N-formylmorpholine with some halobenzenes at 303.15, 308.15 and 313.15 K
n0	1.51072		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	[1062.80; 1117.29]	kg/m3	[283.15; 333.15]
ρl	1117.29	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	1111.81	kg/m3	288.15	Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
ρl	1111.81	kg/m3	288.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1111.89	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	1106.00	kg/m3	293.00	KDB
ρl	1106.00	kg/m3	293.15	Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
ρl	1106.49	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	1106.43	kg/m3	293.15	Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
ρl	1106.43	kg/m3	293.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1106.55	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	1106.07	kg/m3	293.20	Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
ρl	1101.08	kg/m3	298.00	Optimization of liquid-liquid equilibria of the type 2 ternary systems (water + valeric acid + aromatic solvent): Modeling through SERLAS
ρl	1100.80	kg/m3	298.15	Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
ρl	1100.90	kg/m3	298.15	Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
ρl	1101.16	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	1101.04	kg/m3	298.15	Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
ρl	1101.04	kg/m3	298.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1101.03	kg/m3	298.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
ρl	1101.17	kg/m3	298.15	Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
ρl	1101.08	kg/m3	298.20	Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
ρl	1095.64	kg/m3	303.15	Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
ρl	1095.54	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	1095.49	kg/m3	303.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
ρl	1095.52	kg/m3	303.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
ρl	1095.70	kg/m3	303.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl	1095.71	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	1086.60	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	1095.79	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	1095.64	kg/m3	303.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1090.23	kg/m3	308.15	Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
ρl	1090.20	kg/m3	308.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
ρl	1090.23	kg/m3	308.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1085.10	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	1089.72	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	1084.82	kg/m3	313.15	Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
ρl	1081.10	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	1084.80	kg/m3	313.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl	1084.86	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	1084.82	kg/m3	313.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1084.71	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	1079.45	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	1079.42	kg/m3	318.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1073.80	kg/m3	323.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl	1073.96	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	1073.97	kg/m3	323.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	1063.01	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
ρl	1062.80	kg/m3	333.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ΔfusS	[41.93; 41.93]	J/mol×K	[227.89; 227.89]
ΔfusS	41.93	J/mol×K	227.89	NIST
ΔfusS	41.93	J/mol×K	227.89	NIST
γ	[0.03; 0.03]	N/m	[293.20; 323.15]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	303.15	Thermophysical Properties of para-Anisaldehyde (1) + Chlorobenzene (2) at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
γ	0.03	N/m	313.15	Thermophysical Properties of para-Anisaldehyde (1) + Chlorobenzene (2) at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
γ	0.03	N/m	323.15	Thermophysical Properties of para-Anisaldehyde (1) + Chlorobenzene (2) 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)	404.35	K	95.30	Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
Tfus(P)	[246.40; 530.87]	K	[100000.00; 3500000.00]
Tfus(P)	246.40	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)	263.03	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)	273.46	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)	288.44	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)	301.03	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)	315.62	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)	325.56	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)	336.87	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)	348.81	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)	354.76	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)	403.44	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)	440.81	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)	473.28	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)	503.63	K	3000000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
Tfus(P)	530.87	K	3500000.00	Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa

Datasets

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	1251.8
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[79.89; 254.83]	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			7.46800e+01
Coefficient B			-1.00150e+03
Coefficient C			6.91924e+00
Coefficient D			-1.40140e-03
Coefficient E			4.64130e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	79.89	J/mol×K	200.00	Calculated Property
Cp,gas	110.70	J/mol×K	344.44	Calculated Property
Cp,gas	148.12	J/mol×K	488.89	Calculated Property
Cp,gas	177.87	J/mol×K	633.33	Calculated Property
Cp,gas	198.94	J/mol×K	777.78	Calculated Property
Cp,gas	213.84	J/mol×K	922.22	Calculated Property
Cp,gas	225.12	J/mol×K	1066.67	Calculated Property
Cp,gas	234.79	J/mol×K	1211.11	Calculated Property
Cp,gas	244.31	J/mol×K	1355.56	Calculated Property
Cp,gas	254.83	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[142.73; 179.08]	J/mol×K	[227.95; 360.00]	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			1.39150e+02
Coefficient B			-3.33420e+02
Coefficient C			3.99824e+00
Coefficient D			-1.80360e-02
Coefficient E			5.48460e-05
Temperature range, min.			227.95
Temperature range, max.			360.00
Cp,liquid	142.73	J/mol×K	227.95	Calculated Property
Cp,liquid	143.53	J/mol×K	242.62	Calculated Property
Cp,liquid	144.58	J/mol×K	257.29	Calculated Property
Cp,liquid	146.00	J/mol×K	271.97	Calculated Property
Cp,liquid	147.92	J/mol×K	286.64	Calculated Property
Cp,liquid	150.58	J/mol×K	301.31	Calculated Property
Cp,liquid	154.33	J/mol×K	315.98	Calculated Property
Cp,liquid	159.70	J/mol×K	330.66	Calculated Property
Cp,liquid	167.51	J/mol×K	345.33	Calculated Property
Cp,liquid	179.08	J/mol×K	360.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0014289; 0.0001120]	Pa×s	[250.00; 573.00]	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			2.94830e-02
Coefficient B			5.56490e+02
Coefficient C			-1.59630e+00
Coefficient D			1.21710e-07
Coefficient E			2.00000e+00
Temperature range, min.			250.00
Temperature range, max.			573.00
η	0.0014289	Pa×s	250.00	Calculated Property
η	0.0008743	Pa×s	285.89	Calculated Property
η	0.0005842	Pa×s	321.78	Calculated Property
η	0.0004161	Pa×s	357.67	Calculated Property
η	0.0003109	Pa×s	393.56	Calculated Property
η	0.0002412	Pa×s	429.44	Calculated Property
η	0.0001928	Pa×s	465.33	Calculated Property
η	0.0001578	Pa×s	501.22	Calculated Property
η	0.0001318	Pa×s	537.11	Calculated Property
η	0.0001120	Pa×s	573.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[43.50; 1.78]	kJ/mol	[227.95; 632.35]	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			4.90390e+01
Coefficient B			2.44730e-01
Coefficient C			-4.86520e-02
Coefficient D			4.05370e-01
Coefficient E			-2.50120e-01
Critical temperature, Tc (K)			6.32400e+02
Temperature range, min.			227.95
Temperature range, max.			632.35
ΔvapH	43.50	kJ/mol	227.95	Calculated Property
ΔvapH	41.89	kJ/mol	272.88	Calculated Property
ΔvapH	40.02	kJ/mol	317.82	Calculated Property
ΔvapH	37.88	kJ/mol	362.75	Calculated Property
ΔvapH	35.41	kJ/mol	407.68	Calculated Property
ΔvapH	32.55	kJ/mol	452.62	Calculated Property
ΔvapH	29.20	kJ/mol	497.55	Calculated Property
ΔvapH	25.10	kJ/mol	542.48	Calculated Property
ΔvapH	19.50	kJ/mol	587.42	Calculated Property
ΔvapH	1.78	kJ/mol	632.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[293.56; 432.78]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45006e+01
Coefficient B			-3.61917e+03
Coefficient C			-3.89210e+01
Temperature range, min.			293.56
Temperature range, max.			432.78
Pvap	1.33	kPa	293.56	Calculated Property
Pvap	3.01	kPa	309.03	Calculated Property
Pvap	6.22	kPa	324.50	Calculated Property
Pvap	11.92	kPa	339.97	Calculated Property
Pvap	21.46	kPa	355.44	Calculated Property
Pvap	36.56	kPa	370.90	Calculated Property
Pvap	59.40	kPa	386.37	Calculated Property
Pvap	92.60	kPa	401.84	Calculated Property
Pvap	139.20	kPa	417.31	Calculated Property
Pvap	202.67	kPa	432.78	Calculated Property
Pvap	[9.43e-03; 4392.59]	kPa	[227.95; 632.35]	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			4.45056e+01
Coefficient B			-6.02054e+03
Coefficient C			-4.20414e+00
Coefficient D			1.29385e-06
Coefficient E			2.00000e+00
Temperature range, min.			227.95
Temperature range, max.			632.35
Pvap	9.43e-03	kPa	227.95	Calculated Property
Pvap	0.35	kPa	272.88	Calculated Property
Pvap	4.35	kPa	317.82	Calculated Property
Pvap	27.14	kPa	362.75	Calculated Property
Pvap	108.20	kPa	407.68	Calculated Property
Pvap	317.50	kPa	452.62	Calculated Property
Pvap	749.24	kPa	497.55	Calculated Property
Pvap	1507.63	kPa	542.48	Calculated Property
Pvap	2692.86	kPa	587.42	Calculated Property
Pvap	4392.59	kPa	632.35	Calculated Property
Pvap	[9.25e-03; 4404.58]	kPa	[227.95; 632.35]	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			5.24220e+01
Coefficient B			-6.32735e+03
Coefficient C			-5.42919e+00
Coefficient D			2.47507e-06
Coefficient E			0.00000e+00
Temperature range, min.			227.95
Temperature range, max.			632.35
Pvap	9.25e-03	kPa	227.95	Calculated Property
Pvap	0.36	kPa	272.88	Calculated Property
Pvap	4.41	kPa	317.82	Calculated Property
Pvap	27.30	kPa	362.75	Calculated Property
Pvap	107.88	kPa	407.68	Calculated Property
Pvap	314.15	kPa	452.62	Calculated Property
Pvap	738.14	kPa	497.55	Calculated Property
Pvap	1485.81	kPa	542.48	Calculated Property
Pvap	2669.18	kPa	587.42	Calculated Property
Pvap	4404.58	kPa	632.35	Calculated Property
Pvap	[9.65; 101.40]	kPa	[335.19; 404.88]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40707e+01
Coefficient B			-3.30576e+03
Coefficient C			-5.51240e+01
Reference			Brown, 1952, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			335.19
Temperature range, max.			404.88
Pvap	9.65	kPa	335.19	Calculated Property
Pvap	13.26	kPa	342.93	Calculated Property
Pvap	17.92	kPa	350.68	Calculated Property
Pvap	23.84	kPa	358.42	Calculated Property
Pvap	31.27	kPa	366.16	Calculated Property
Pvap	40.48	kPa	373.91	Calculated Property
Pvap	51.76	kPa	381.65	Calculated Property
Pvap	65.44	kPa	389.39	Calculated Property
Pvap	81.87	kPa	397.14	Calculated Property
Pvap	101.40	kPa	404.88	Calculated Property
Pvap	[9.65; 101.40]	kPa	[335.19; 404.88]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40707e+01
Coefficient B			-3.30576e+03
Coefficient C			-5.51240e+01
Reference			Brown, 1952
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			335.19
Temperature range, max.			404.88
Pvap	9.65	kPa	335.19	Calculated Property
Pvap	13.26	kPa	342.93	Calculated Property
Pvap	17.92	kPa	350.68	Calculated Property
Pvap	23.84	kPa	358.42	Calculated Property
Pvap	31.27	kPa	366.16	Calculated Property
Pvap	40.48	kPa	373.91	Calculated Property
Pvap	51.76	kPa	381.65	Calculated Property
Pvap	65.44	kPa	389.39	Calculated Property
Pvap	81.87	kPa	397.14	Calculated Property
Pvap	101.40	kPa	404.88	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1167.40; 387.69]	kg/m3	[227.95; 632.35]	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			8.81174e+01
Coefficient B			2.54640e-01
Coefficient C			6.32400e+02
Coefficient D			2.63420e-01
Temperature range, min.			227.95
Temperature range, max.			632.35
ρl	1167.40	kg/m3	227.95	Calculated Property
ρl	1124.83	kg/m3	272.88	Calculated Property
ρl	1079.93	kg/m3	317.82	Calculated Property
ρl	1032.12	kg/m3	362.75	Calculated Property
ρl	980.58	kg/m3	407.68	Calculated Property
ρl	923.98	kg/m3	452.62	Calculated Property
ρl	860.09	kg/m3	497.55	Calculated Property
ρl	784.35	kg/m3	542.48	Calculated Property
ρl	684.29	kg/m3	587.42	Calculated Property
ρl	387.69	kg/m3	632.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[227.85; 404.85]	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			6.85022e-02
Coefficient B			-1.19100e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			227.85
Temperature range, max.			404.85
γ	0.04	N/m	227.85	Calculated Property
γ	0.04	N/m	247.52	Calculated Property
γ	0.04	N/m	267.18	Calculated Property
γ	0.03	N/m	286.85	Calculated Property
γ	0.03	N/m	306.52	Calculated Property
γ	0.03	N/m	326.18	Calculated Property
γ	0.03	N/m	345.85	Calculated Property
γ	0.02	N/m	365.52	Calculated Property
γ	0.02	N/m	385.18	Calculated Property
γ	0.02	N/m	404.85	Calculated Property
γ	[0.04; 1.64e-05]	N/m	[227.95; 629.11]	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			-9.58240e-03
Coefficient B			1.01650e+02
Coefficient C			-3.60630e+00
Coefficient D			2.40210e-03
Coefficient E			-6.85370e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 632.35 K.
Temperature range, min.			227.95
Temperature range, max.			629.11
γ	0.04	N/m	227.95	Calculated Property
γ	0.04	N/m	272.52	Calculated Property
γ	0.03	N/m	317.10	Calculated Property
γ	0.03	N/m	361.67	Calculated Property
γ	0.02	N/m	406.25	Calculated Property
γ	0.02	N/m	450.82	Calculated Property
γ	0.01	N/m	495.39	Calculated Property
γ	0.01	N/m	539.97	Calculated Property
γ	0.00	N/m	584.54	Calculated Property
γ	1.64e-05	N/m	629.11	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.08]	W/m×K	[227.95; 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			4.16700e-04
Coefficient B			9.20330e-01
Coefficient C			1.90290e+03
Coefficient D			1.23750e+05
Temperature range, min.			227.95
Temperature range, max.			1000.00
λgas	0.01	W/m×K	227.95	Calculated Property
λgas	0.01	W/m×K	313.73	Calculated Property
λgas	0.02	W/m×K	399.52	Calculated Property
λgas	0.02	W/m×K	485.30	Calculated Property
λgas	0.03	W/m×K	571.08	Calculated Property
λgas	0.04	W/m×K	656.87	Calculated Property
λgas	0.05	W/m×K	742.65	Calculated Property
λgas	0.06	W/m×K	828.43	Calculated Property
λgas	0.07	W/m×K	914.22	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.11]	W/m×K	[227.95; 404.87]	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			8.34270e-02
Coefficient B			-1.57940e+02
Coefficient C			-8.97240e-01
Coefficient D			-4.92590e-03
Coefficient E			-2.75890e-06
Temperature range, min.			227.95
Temperature range, max.			404.87
λliquid	0.14	W/m×K	227.95	Calculated Property
λliquid	0.14	W/m×K	247.61	Calculated Property
λliquid	0.13	W/m×K	267.27	Calculated Property
λliquid	0.13	W/m×K	286.92	Calculated Property
λliquid	0.12	W/m×K	306.58	Calculated Property
λliquid	0.12	W/m×K	326.24	Calculated Property
λliquid	0.12	W/m×K	345.90	Calculated Property
λliquid	0.11	W/m×K	365.55	Calculated Property
λliquid	0.11	W/m×K	385.21	Calculated Property
λliquid	0.11	W/m×K	404.87	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, chloro-.

Mixtures

• 1,2-Ethanediol + Benzene, chloro-
• Benzene, chloro- + Pentanoic acid + Water
• Benzene, chloro- + 2,2',4,4',6,6'-Hexanitrobiphenyl
• Benzene, chloro- + Methyl Alcohol
• Ethanol + Benzene, chloro-
• Benzene, chloro- + Pentane, 2,2,4-trimethyl-
• Benzene, chloro- + Bis(2-ethylhexyl)hydrogen phosphate
• Benzenamine, 4-methyl-2-nitro- + Benzene, chloro-
• Benzene, chloro- + 1-Hexanol
• Benzene, chloro- + Triethylamine
• Benzene, chloro- + Furan, tetrahydro-2-methyl-
• Benzene + Benzene, chloro- + Cyclohexane
• Formamide, N,N-dimethyl- + Benzene, chloro-
• Benzene, bromo- + Benzene, chloro-
• Benzene, nitro- + Benzene, chloro-
• Benzene, bromo- + Benzene, chloro- + Ethane, 1,2-dichloro-
• Benzene, nitro- + Benzene, chloro- + Ethane, 1,2-dichloro-
• Benzene, chloro- + Benzene, ethyl-
• Benzene, chloro- + Dimethyl Sulfoxide
• Benzene, chloro- + m-Chloroaniline

Find more mixtures with Benzene, chloro-.

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• 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 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
• 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.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• 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
• Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
• Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
• Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
• Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
• Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
• Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
• Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
• Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
• Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
• 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
• Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
• Ionic liquid structural effects on solute partitioning in biphasic ionic liquid and supercritical carbon dioxide systems
• Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
• Solubility of elemental sulfur in pure organic solvents and organic solvent-ionic liquid mixtures from 293.15 to 353.15 K
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
• Refractive properties, speed of sound and FT-IR study of binary mixtures of N-formylmorpholine with some halobenzenes at 303.15, 308.15 and 313.15 K
• Phase equilibrium for ternary liquid systems of water + di-(2- ethylhexyl)phosphoric acid + organic diluents: Thermodynamic study
• Measurement of infinite dilution partition coefficients of isomeric benzene derivatives in [bmim][Tf2N]-CO2 biphasic system and correlation with the ePC-SAFT equation of state
• Optimization of liquid-liquid equilibria of the type 2 ternary systems (water + valeric acid + aromatic solvent): Modeling through SERLAS
• Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
• Determination and correlation of solubility of 2,2',4,4',6,6 '-hexanitro-1,1'-biphenyl and 2,2',2" ,4,4',4" ,6,6',6" -Nonanitro-1,1 ':3',1"-terphenyl in six pure solvents
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• Phase equilibria for ternary liquid systems of (water + tetrahydrofuran + nonprotic aromatic solvent) at T = 298.2 K
• Azeotropic behaviour of (benzene + cyclohexane + chlorobenzene) ternary mixture using chlorobenzene as entrainer at 101.3 kPa
• Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Thermodynamics of solvation and solvophobic effect in formamide
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
• Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
• Ultrasonic and 31P NMR investigations of an acidic nuclear extractant with some monosubstituted benzenes
• 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
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• 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
• Thermophysical properties of the binary mixtures of 2-methyl-tetrahydrofuran with benzene and halobenzenes
• Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
• 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
• Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
• Dilute Vapor Absorption: A New Accurate Technique for Measurement of the Limiting Activity Coefficient of Water in Hydrophobic Solvents of Lower Volatility
• The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
• Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
• Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile
• Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
• Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
• 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
• Densities, Viscosities, and Thermodynamic Properties of (N,N-Dimethylformamide + Benzene + Chlorobenzene) Ternary Mixtures at (298.15, 303.15, 308.15, and 313.15) K
• Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
• Pressure-Density-Temperature Behavior of CO2/Acetone, CO2/Toluene, and CO2/Monochlorobenzene Mixtures in the Near-Critical Region
• Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
• Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
• Solubilities of 2-(2-Hydroxyphenyl)phenylphosphonic Acid in Chlorobenzene and in Water and Partition Coefficient between Water + Chlorobenzene Mixtures
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Vapor Pressure Measurements for 2-Chloromethylbenzoxazole and Vapor-Liquid Equilibrium Measurements for the Chlorobenzene + 2-Chloromethylbenzoxazole System
• Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
• Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
• Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
• Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
• Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
• Solubility of Hydrofluorocarbons in Halobenzene Solvents
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
• Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
• 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
• Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
• Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
• Thermophysical Properties of para-Anisaldehyde (1) + Chlorobenzene (2) at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
• Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
• Liquid-Liquid Equilibria in Binary Mixtures Containing Chlorobenzene, Bromobenzene, and Iodobenzene with Ionic Liquid 1-Ethyl-3-methylimidazolim Bis(trifluoromethylsulfonyl)imide
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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