Chemical Properties of Benzene, 1,2-dichloro- (CAS 95-50-1)

InChI

InChI=1S/C6H4Cl2/c7-5-3-1-2-4-6(5)8/h1-4H

InChI Key

RFFLAFLAYFXFSW-UHFFFAOYSA-N

Formula

C6H4Cl2

SMILES

Clc1ccccc1Cl

Molecular Weight¹

147.00

CAS

95-50-1

Other Names

• 1,2-Dichlorbenzene
• 1,2-dichlorobenzene
• Benzene, o-dichloro-
• Chloroben
• Chloroden
• Cloroben
• DCB
• Dichlorobenzene, o-
• Dichlorobenzene, ortho
• Dilantin DB
• Dilatin db
• Dizene
• Dowtherm E
• NCI-C54944
• NSC 60644
• ODB
• ODCB
• Orthodichlorobenzol
• Special termite fluid
• Termitkil
• UN 1591
• o-Dichlorbenzene
• o-Dichlorbenzol
• o-Dichlorobenzol
• o-dichlorobenzene
• ortho-Dichlorobenzene

• ω : Acentric Factor.
• 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_fH°_{(+) ion} : Enthalpy of formation of positive ion at standard conditions (kJ/mol).
• Δ_fH_{(+) ion,0K} : Enthalpy of formation of positive ion at 0K (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_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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced 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_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	[0.2192; 0.2720]
ω	0.2720		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2192		ChemSep v8.3 pure component data Compiled value
ω	0.2720		KDB
ΔcH°liquid	[-2964.70; -2957.80]	kJ/mol
ΔcH°liquid	-2964.70	kJ/mol	NIST
ΔcH°liquid	-2962.60 ± 1.30	kJ/mol	NIST
ΔcH°liquid	-2963.00 ± 2.00	kJ/mol	NIST
ΔcH°liquid	-2958.60 ± 0.71	kJ/mol	NIST
ΔcH°liquid	-2963.90 ± 2.50	kJ/mol	NIST
ΔcH°liquid	-2957.80 ± 1.20	kJ/mol	NIST
μ	[2.30; 2.50]	debye
μ	2.50	debye	ChemSep v8.3 pure component data Compiled value
μ	2.30	debye	KDB
EA	0.09	eV	NIST
ΔfG°	[82.73; 82.90]	kJ/mol
ΔfG°	82.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	82.73	kJ/mol	KDB
ΔfH°gas	[30.00; 33.00]	kJ/mol
ΔfH°gas	30.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	30.00	kJ/mol	KDB
ΔfH°gas	33.00	kJ/mol	NIST
ΔfH°liquid	[-17.60; -16.00]	kJ/mol
ΔfH°liquid	-17.40 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-16.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-17.60 ± 0.71	kJ/mol	NIST
ΔfH°(+) ion	904.20	kJ/mol	NIST
ΔfH(+) ion,0K	916.70	kJ/mol	NIST
ΔfusH°	13.34	kJ/mol	Joback Calculated Property
ΔvapH°	[48.50; 50.90]	kJ/mol
ΔvapH°	50.90	kJ/mol	NIST
ΔvapH°	48.50 ± 0.10	kJ/mol	NIST
ΔvapH°	49.90	kJ/mol	NIST
IE	[9.06; 9.24]	eV
IE	9.06 ± 0.02	eV	NIST
IE	9.06 ± 0.02	eV	NIST
IE	9.08 ± 0.03	eV	NIST
IE	9.06 ± 0.02	eV	NIST
IE	9.08 ± 0.01	eV	NIST
IE	9.07 ± 0.01	eV	NIST
IE	9.06	eV	NIST
IE	Outlier 9.24	eV	NIST
IE	9.23	eV	NIST
IE	9.08	eV	NIST
log10WS	[-3.05; -3.03]
log10WS	-3.03		Aq. Solubility Prediction
log10WS	-3.05		Estimated Solubility
logPoct/wat	2.993		Crippen Calculated Property
McVol	96.120	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	2		KDB
Pc	[4070.00; 4103.66]	kPa
Pc	4103.66	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4070.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4100.00	kPa	KDB
Ptriple	6.49e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[167.40; 1076.00]
Inp	1013.00		NIST
Inp	1028.00		NIST
Inp	1046.17		NIST
Inp	1046.22		NIST
Inp	1056.93		NIST
Inp	1057.07		NIST
Inp	1050.00		NIST
Inp	1063.80		NIST
Inp	1063.80		NIST
Inp	1074.00		NIST
Inp	1035.00		NIST
Inp	1052.48		NIST
Inp	1031.00		NIST
Inp	1040.29		NIST
Inp	1005.00		NIST
Inp	1050.00		NIST
Inp	1045.00		NIST
Inp	1005.00		NIST
Inp	1038.00		NIST
Inp	1050.00		NIST
Inp	1021.00		NIST
Inp	1076.00		NIST
Inp	1013.00		NIST
Inp	1019.00		NIST
Inp	1024.00		NIST
Inp	1045.72		NIST
Inp	1046.00		NIST
Inp	1049.02		NIST
Inp	1049.74		NIST
Inp	1002.80		NIST
Inp	1022.40		NIST
Inp	1030.00		NIST
Inp	1012.20		NIST
Inp	1021.95		NIST
Inp	1025.52		NIST
Inp	1029.19		NIST
Inp	1030.00		NIST
Inp	1025.00		NIST
Inp	1016.00		NIST
Inp	1016.00		NIST
Inp	1009.00		NIST
Inp	1028.00		NIST
Inp	1031.00		NIST
Inp	1015.00		NIST
Inp	1033.00		NIST
Inp	1012.00		NIST
Inp	1010.00		NIST
Inp	1013.00		NIST
Inp	1014.40		NIST
Inp	1003.00		NIST
Inp	1027.00		NIST
Inp	992.00		NIST
Inp	995.00		NIST
Inp	1013.00		NIST
Inp	1030.00		NIST
Inp	986.00		NIST
Inp	984.00		NIST
Inp	1007.00		NIST
Inp	1005.00		NIST
Inp	1006.00		NIST
Inp	1031.00		NIST
Inp	1007.00		NIST
Inp	1008.00		NIST
Inp	1067.00		NIST
Inp	1055.00		NIST
Inp	1007.00		NIST
Inp	1009.00		NIST
Inp	1030.00		NIST
Inp	1031.00		NIST
Inp	Outlier 168.00		NIST
Inp	Outlier 167.40		NIST
Inp	1015.00		NIST
Inp	1007.00		NIST
Inp	1008.00		NIST
Inp	1009.00		NIST
Inp	995.00		NIST
Inp	Outlier 168.00		NIST
Ip	[1445.00; 1529.80]
Ip	1452.00		NIST
Ip	1529.80		NIST
Ip	1445.00		NIST
Ip	1447.00		NIST
Ip	1514.00		NIST
Ip	1486.00		NIST
Ip	1455.00		NIST
Ip	1459.00		NIST
Ip	1492.00		NIST
Ip	1492.00		NIST
Ip	1519.77		NIST
Ip	1511.85		NIST
Ip	1488.07		NIST
Ip	1495.00		NIST
Ip	1497.00		NIST
Ip	1452.00		NIST
Ip	1492.00		NIST
Ip	1495.00		NIST
Ip	1486.00		NIST
Ip	1529.80		NIST
Tboil	[452.65; 453.70]	K
Tboil	453.57	K	ChemSep v8.3 pure component data Compiled value
Tboil	453.60	K	KDB
Tboil	453.70	K	NIST
Tboil	453.40 ± 0.50	K	NIST
Tboil	453.00 ± 1.50	K	NIST
Tboil	453.63 ± 0.07	K	NIST
Tboil	452.65 ± 0.35	K	NIST
Tc	[697.30; 729.00]	K
Tc	698.80	K	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
Tc	729.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	697.30	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	705.00	K	ChemSep v8.3 pure component data Compiled value
Tc	729.00	K	KDB
Tfus	[255.20; 256.15]	K
Tfus	256.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	256.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	256.10	K	KDB
Tfus	255.92	K	Aq. Solubility Prediction
Tfus	Outlier 255.20 ± 0.20	K	NIST
Tfus	256.15 ± 0.05	K	NIST
Tfus	256.00 ± 0.10	K	NIST
Tfus	256.13 ± 0.10	K	NIST
Tfus	256.14 ± 0.05	K	NIST
Tfus	256.12 ± 0.05	K	NIST
Tfus	256.00 ± 2.00	K	NIST
Tfus	256.00 ± 0.50	K	NIST
Ttriple	256.15	K	ChemSep v8.3 pure component data Compiled value
UQi	3.29		ChemSep v8.3 pure component data Compiled value
URi	4.44		ChemSep v8.3 pure component data Compiled value
Vc	[0.351; 0.360]	m3/kmol
Vc	0.360	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.351	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.360	m3/kmol	KDB
Zc	[0.2435130; 0.2440000]
Zc	0.2440000		ChemSep v8.3 pure component data Compiled value
Zc	0.2435130		KDB
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[167.68; 183.28]	J/mol×K	[283.15; 353.15]
Cp,liquid	167.68	J/mol×K	283.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	168.06	J/mol×K	285.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	168.44	J/mol×K	287.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	168.83	J/mol×K	289.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	169.23	J/mol×K	291.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	169.64	J/mol×K	293.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	170.05	J/mol×K	295.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	170.47	J/mol×K	297.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	170.90	J/mol×K	298.15	NIST
Cp,liquid	170.89	J/mol×K	299.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	171.32	J/mol×K	301.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	171.76	J/mol×K	303.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	172.20	J/mol×K	305.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	172.64	J/mol×K	307.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	173.09	J/mol×K	309.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	173.54	J/mol×K	311.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	174.00	J/mol×K	313.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	174.46	J/mol×K	315.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	174.92	J/mol×K	317.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	175.38	J/mol×K	319.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	175.85	J/mol×K	321.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	176.32	J/mol×K	323.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	176.79	J/mol×K	325.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	177.26	J/mol×K	327.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	177.73	J/mol×K	329.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	178.20	J/mol×K	331.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	178.67	J/mol×K	333.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	179.14	J/mol×K	335.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	179.61	J/mol×K	337.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	180.07	J/mol×K	339.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	180.54	J/mol×K	341.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	181.00	J/mol×K	343.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	181.47	J/mol×K	345.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	181.92	J/mol×K	347.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	182.38	J/mol×K	349.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	182.83	J/mol×K	351.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	183.28	J/mol×K	353.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
ΔfusH	[12.40; 12.93]	kJ/mol	[255.65; 256.50]
ΔfusH	12.92	kJ/mol	255.65	NIST
ΔfusH	12.40	kJ/mol	255.90	NIST
ΔfusH	12.93	kJ/mol	256.50	NIST
ΔfusH	12.93	kJ/mol	256.50	NIST
ΔvapH	[39.66; 51.20]	kJ/mol	[256.00; 449.10]
ΔvapH	51.20	kJ/mol	256.00	NIST
ΔvapH	50.80	kJ/mol	271.50	NIST
ΔvapH	51.20	kJ/mol	285.50	NIST
ΔvapH	50.00	kJ/mol	322.00	NIST
ΔvapH	44.50	kJ/mol	408.50	NIST
ΔvapH	44.00	kJ/mol	413.00	NIST
ΔvapH	39.66	kJ/mol	449.10	KDB
Pvap	[4.86; 98.36]	kPa	[360.41; 452.62]
Pvap	4.86	kPa	360.41	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	9.95	kPa	377.35	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	14.98	kPa	388.41	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	20.04	kPa	396.96	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	24.99	kPa	403.40	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	30.00	kPa	408.91	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	35.02	kPa	414.16	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	40.02	kPa	418.75	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	45.05	kPa	422.87	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	55.03	kPa	429.99	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	59.97	kPa	433.29	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	69.93	kPa	438.87	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	79.98	kPa	443.92	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	90.20	kPa	448.94	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	95.11	kPa	451.11	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
Pvap	98.36	kPa	452.62	Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
n0	[1.53320; 1.55230]		[288.20; 328.20]
n0	1.55230		288.20	Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
n0	1.54600		298.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
n0	1.54910		298.15	Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
n0	1.54990		298.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0	1.54890		298.20	Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
n0	1.54400		303.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
n0	1.54760		303.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0	1.54100		308.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
n0	1.54500		308.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0	1.54380		308.20	Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
n0	1.53860		318.20	Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
n0	1.53320		328.20	Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
ρl	[1299.20; 1306.00]	kg/m3	[293.00; 303.15]
ρl	1306.00	kg/m3	293.00	KDB
ρl	1299.20	kg/m3	303.15	Effect of various substituents on benzene ring and their impact on volumetric, acoustic and transport properties of binary liquid mixtures with dimethylacetamide
ΔfusS	50.50	J/mol×K	255.65	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	451.20	K	102.00	NIST

Datasets

Viscosity, Pa*s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	303.15	0.0013
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[81.72; 251.83]	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			5.55600e+01
Coefficient B			-4.90510e+02
Coefficient C			5.74024e+00
Coefficient D			-1.21860e-04
Coefficient E			2.17920e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	81.72	J/mol×K	200.00	Calculated Property
Cp,gas	127.57	J/mol×K	344.44	Calculated Property
Cp,gas	163.61	J/mol×K	488.89	Calculated Property
Cp,gas	189.49	J/mol×K	633.33	Calculated Property
Cp,gas	208.19	J/mol×K	777.78	Calculated Property
Cp,gas	221.98	J/mol×K	922.22	Calculated Property
Cp,gas	232.39	J/mol×K	1066.67	Calculated Property
Cp,gas	240.42	J/mol×K	1211.11	Calculated Property
Cp,gas	246.75	J/mol×K	1355.56	Calculated Property
Cp,gas	251.83	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[156.80; 256.20]	J/mol×K	[266.02; 528.75]	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			1.27840e+02
Coefficient B			-5.91560e+01
Coefficient C			1.46504e+00
Coefficient D			9.35690e-03
Coefficient E			-5.17140e-06
Temperature range, min.			266.02
Temperature range, max.			528.75
Cp,liquid	156.80	J/mol×K	266.02	Calculated Property
Cp,liquid	163.58	J/mol×K	295.21	Calculated Property
Cp,liquid	171.39	J/mol×K	324.40	Calculated Property
Cp,liquid	180.28	J/mol×K	353.60	Calculated Property
Cp,liquid	190.30	J/mol×K	382.79	Calculated Property
Cp,liquid	201.44	J/mol×K	411.98	Calculated Property
Cp,liquid	213.68	J/mol×K	441.17	Calculated Property
Cp,liquid	226.96	J/mol×K	470.37	Calculated Property
Cp,liquid	241.18	J/mol×K	499.56	Calculated Property
Cp,liquid	256.20	J/mol×K	528.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0027334; 0.0003714]	Pa×s	[256.15; 453.57]	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			-3.76990e+01
Coefficient B			2.37700e+03
Coefficient C			4.08480e+00
Coefficient D			-2.07680e-06
Coefficient E			2.00000e+00
Temperature range, min.			256.15
Temperature range, max.			453.57
η	0.0027334	Pa×s	256.15	Calculated Property
η	0.0017947	Pa×s	278.09	Calculated Property
η	0.0012759	Pa×s	300.02	Calculated Property
η	0.0009644	Pa×s	321.96	Calculated Property
η	0.0007647	Pa×s	343.89	Calculated Property
η	0.0006297	Pa×s	365.83	Calculated Property
η	0.0005345	Pa×s	387.76	Calculated Property
η	0.0004648	Pa×s	409.70	Calculated Property
η	0.0004122	Pa×s	431.63	Calculated Property
η	0.0003714	Pa×s	453.57	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[51.11; 0.00]	kJ/mol	[256.15; 705.00]	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			8.77400e+01
Coefficient B			2.82270e+00
Coefficient C			-6.84330e+00
Coefficient D			7.65470e+00
Coefficient E			-3.12750e+00
Critical temperature, Tc (K)			7.05000e+02
Temperature range, min.			256.15
Temperature range, max.			705.00
ΔvapH	51.11	kJ/mol	256.15	Calculated Property
ΔvapH	48.57	kJ/mol	306.02	Calculated Property
ΔvapH	46.07	kJ/mol	355.89	Calculated Property
ΔvapH	43.32	kJ/mol	405.77	Calculated Property
ΔvapH	40.12	kJ/mol	455.64	Calculated Property
ΔvapH	36.33	kJ/mol	505.51	Calculated Property
ΔvapH	31.88	kJ/mol	555.38	Calculated Property
ΔvapH	26.59	kJ/mol	605.26	Calculated Property
ΔvapH	19.70	kJ/mol	655.13	Calculated Property
ΔvapH	0.00	kJ/mol	705.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[330.74; 484.72]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40308e+01
Coefficient B			-3.67273e+03
Coefficient C			-6.35030e+01
Temperature range, min.			330.74
Temperature range, max.			484.72
Pvap	1.33	kPa	330.74	Calculated Property
Pvap	3.05	kPa	347.85	Calculated Property
Pvap	6.34	kPa	364.96	Calculated Property
Pvap	12.20	kPa	382.07	Calculated Property
Pvap	21.96	kPa	399.18	Calculated Property
Pvap	37.34	kPa	416.28	Calculated Property
Pvap	60.44	kPa	433.39	Calculated Property
Pvap	93.74	kPa	450.50	Calculated Property
Pvap	140.10	kPa	467.61	Calculated Property
Pvap	202.66	kPa	484.72	Calculated Property
Pvap	[6.04e-03; 2858.86]	kPa	[256.15; 705.00]	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			6.88521e+01
Coefficient B			-8.22676e+03
Coefficient C			-7.55275e+00
Coefficient D			6.19130e-07
Coefficient E			2.00000e+00
Temperature range, min.			256.15
Temperature range, max.			705.00
Pvap	6.04e-03	kPa	256.15	Calculated Property
Pvap	0.30	kPa	306.02	Calculated Property
Pvap	4.24	kPa	355.89	Calculated Property
Pvap	27.64	kPa	405.77	Calculated Property
Pvap	108.80	kPa	455.64	Calculated Property
Pvap	303.67	kPa	505.51	Calculated Property
Pvap	664.78	kPa	555.38	Calculated Property
Pvap	1219.71	kPa	605.26	Calculated Property
Pvap	1962.51	kPa	655.13	Calculated Property
Pvap	2858.86	kPa	705.00	Calculated Property
Pvap	[6.43e-03; 4105.80]	kPa	[256.15; 729.00]	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			6.74184e+01
Coefficient B			-8.04769e+03
Coefficient C			-7.42072e+00
Coefficient D			1.61077e-06
Coefficient E			0.00000e+00
Temperature range, min.			256.15
Temperature range, max.			729.00
Pvap	6.43e-03	kPa	256.15	Calculated Property
Pvap	0.35	kPa	308.69	Calculated Property
Pvap	5.18	kPa	361.23	Calculated Property
Pvap	34.20	kPa	413.77	Calculated Property
Pvap	135.79	kPa	466.31	Calculated Property
Pvap	383.70	kPa	518.84	Calculated Property
Pvap	856.26	kPa	571.38	Calculated Property
Pvap	1614.84	kPa	623.92	Calculated Property
Pvap	2694.26	kPa	676.46	Calculated Property
Pvap	4105.80	kPa	729.00	Calculated Property
Pvap	[0.13; 101.32]	kPa	[293.14; 453.57]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42649e+01
Coefficient B			-3.79823e+03
Coefficient C			-5.98360e+01
Reference			McDonald, Shrader, et al., 1959
Temperature range, min.			293.14
Temperature range, max.			453.57
Pvap	0.13	kPa	293.14	Calculated Property
Pvap	0.42	kPa	310.97	Calculated Property
Pvap	1.15	kPa	328.79	Calculated Property
Pvap	2.77	kPa	346.62	Calculated Property
Pvap	6.02	kPa	364.44	Calculated Property
Pvap	12.00	kPa	382.27	Calculated Property
Pvap	22.24	kPa	400.09	Calculated Property
Pvap	38.78	kPa	417.92	Calculated Property
Pvap	64.12	kPa	435.74	Calculated Property
Pvap	101.32	kPa	453.57	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1346.32; 418.13]	kg/m3	[256.15; 705.00]	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			1.09165e+02
Coefficient B			2.61080e-01
Coefficient C			7.05000e+02
Coefficient D			3.06550e-01
Temperature range, min.			256.15
Temperature range, max.			705.00
ρl	1346.32	kg/m3	256.15	Calculated Property
ρl	1291.64	kg/m3	306.02	Calculated Property
ρl	1234.51	kg/m3	355.89	Calculated Property
ρl	1174.34	kg/m3	405.77	Calculated Property
ρl	1110.23	kg/m3	455.64	Calculated Property
ρl	1040.82	kg/m3	505.51	Calculated Property
ρl	963.70	kg/m3	555.38	Calculated Property
ρl	874.09	kg/m3	605.26	Calculated Property
ρl	759.02	kg/m3	655.13	Calculated Property
ρl	418.13	kg/m3	705.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 4.78e-05]	N/m	[256.15; 705.00]	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			-3.37300e-03
Coefficient B			4.82910e+02
Coefficient C			-6.86650e+00
Coefficient D			1.13740e-02
Coefficient E			-1.51200e-05
Temperature range, min.			256.15
Temperature range, max.			705.00
γ	0.04	N/m	256.15	Calculated Property
γ	0.04	N/m	306.02	Calculated Property
γ	0.03	N/m	355.89	Calculated Property
γ	0.03	N/m	405.77	Calculated Property
γ	0.02	N/m	455.64	Calculated Property
γ	0.01	N/m	505.51	Calculated Property
γ	0.01	N/m	555.38	Calculated Property
γ	0.01	N/m	605.26	Calculated Property
γ	0.00	N/m	655.13	Calculated Property
γ	4.78e-05	N/m	705.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.06]	W/m×K	[256.15; 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			-1.20020e+03
Coefficient B			7.23500e-01
Coefficient C			-2.84220e+09
Coefficient D			-8.86840e+10
Temperature range, min.			256.15
Temperature range, max.			1000.00
λgas	0.01	W/m×K	256.15	Calculated Property
λgas	0.01	W/m×K	338.80	Calculated Property
λgas	0.01	W/m×K	421.45	Calculated Property
λgas	0.02	W/m×K	504.10	Calculated Property
λgas	0.02	W/m×K	586.75	Calculated Property
λgas	0.03	W/m×K	669.40	Calculated Property
λgas	0.04	W/m×K	752.05	Calculated Property
λgas	0.04	W/m×K	834.70	Calculated Property
λgas	0.05	W/m×K	917.35	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.13; 0.11]	W/m×K	[262.87; 351.71]	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			6.91900e-02
Coefficient B			-3.79090e+02
Coefficient C			8.99480e-01
Coefficient D			-9.90370e-03
Coefficient E			4.16770e-06
Temperature range, min.			262.87
Temperature range, max.			351.71
λliquid	0.13	W/m×K	262.87	Calculated Property
λliquid	0.13	W/m×K	272.74	Calculated Property
λliquid	0.12	W/m×K	282.61	Calculated Property
λliquid	0.12	W/m×K	292.48	Calculated Property
λliquid	0.12	W/m×K	302.35	Calculated Property
λliquid	0.12	W/m×K	312.23	Calculated Property
λliquid	0.12	W/m×K	322.10	Calculated Property
λliquid	0.12	W/m×K	331.97	Calculated Property
λliquid	0.11	W/m×K	341.84	Calculated Property
λliquid	0.11	W/m×K	351.71	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, 1,2-dichloro-.

Mixtures

• Benzene, 1,2-dichloro- + Dimethyl Sulfoxide
• Benzene, 1,2-dichloro- + N,N-Dimethylacetamide
• Benzene, 1,2-dichloro- + Tetrahydrofuran
• Benzene, 1,2-dichloro- + Formamide
• Benzene, 1,2-dichloro- + 1,2-Ethanediol
• Benzene, 1,2-dichloro- + Propylene Glycol
• n-Hexane + Benzene, 1,2-dichloro- + Furfural
• Benzene, 1,2-dichloro- + Furfural + Hexadecane
• Benzene, 1,2-dichloro- + Water
• Benzene, 1,2-dichloro- + Pentane, 2,2,4-trimethyl-
• Benzene, 1,2-dichloro- + Cyclooctane
• Benzene, 1,2-dichloro- + Octane
• Azacyclotridecan-2-one + Benzene, 1,2-dichloro-
• Benzene, 1,2-dichloro- + 1,4-Dioxane
• Benzene, 1,2-dichloro- + Sulfur, mol. (S8) + Benzene, chloro-
• Benzene, 1,2-dichloro- + Buckminsterfullerene
• Benzene + Benzene, 1,2-dichloro- + Hexane, 1-chloro-
• Benzene, 1,2-dichloro- + Naphthalene
• Benzene, 1,2-dichloro- + Pentanenitrile
• Benzene, 1,2-dichloro- + 2-Octanol

Find more mixtures with Benzene, 1,2-dichloro-.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 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.
• 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
• Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
• Densities and ultrasonic studies for binary mixtures of tetrahydrofuran with chlorobenzenes, chlorotoluenes and nitrotoluenes at 298.15 K
• Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
• Effect of various substituents on benzene ring and their impact on volumetric, acoustic and transport properties of binary liquid mixtures with dimethylacetamide
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Volumetric, ultrasonic and viscometric studies of binary mixtures of dimethyl sulphoxide with chloro and nitro substituted aromatic hydrocarbons at T = 303.15 K
• Thermodynamics of solvation and solvophobic effect in formamide
• S6 Isomer of C60(CF3)12: Synthesis, properties and thermodynamic functions
• Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
• 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
• 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
• Solution and solvation enthalpies of aromatic derivitives in binary mixtures. Dipole moment and dielectric properties
• Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
• 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
• Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
• Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,2-Dichlorobenzene + Benzene +1-Chlorohexane at 298.15 K
• The Effects of Temperature and Inorganic Salts on the Aqueous Solubility of Selected Chlorobenzenes
• Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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