Chemical Properties of Ethane, 1,2-dibromo- (CAS 106-93-4)

InChI

InChI=1S/C2H4Br2/c3-1-2-4/h1-2H2

InChI Key

PAAZPARNPHGIKF-UHFFFAOYSA-N

Formula

C2H4Br2

SMILES

BrCCBr

Molecular Weight¹

187.86

CAS

106-93-4

Other Names

• 1,2-Dibromaethan
• 1,2-Dibromoetano
• 1,2-Dibroomethaan
• 1,2-Ethylene dibromide
• 1,2-dibromoethane
• 1,2-dibromoethane (EDB)
• 1,2-dibromoethyne
• ALPHA,BETA-DIBROMOETHANE
• Aadibroom
• Aethylenbromid
• Bromofume
• Bromuro di etile
• CH2BrCH2Br
• Celmide
• DBE
• Dibromoethane
• Dibromure D'ethylene
• Dowfume 40
• Dowfume W-100
• Dowfume W-8
• Dowfume W-90
• Dowfume W85
• Dowfume edb
• Dwubromoetan
• E-D-Bee
• EDB
• EDB-85
• ENT 15,349
• Edabrom
• Fumo-gas
• Iscobrome D
• Kopfume
• NCI-C00522
• Nefis
• Nephis
• Pestmaster edb-85
• Rcra waste number U067
• Sanhyuum
• Soilbrom
• Soilbrom-100
• Soilbrom-40
• Soilbrom-85
• Soilbrom-90
• Soilbrom-90ec
• Soilbrome-85
• Soilfume
• UN 1605
• Unifume
• alpha,omega-dibromoethane
• ethylene bromide
• ethylene dibromide
• glycol dibromide
• sym-Dibromoethane
• «alpha»,«beta»-Dibromoethane
• «alpha»,«omega»-Dibromoethane

• 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : 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_subH : Enthalpy of sublimation 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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2250; 0.7950]
ω	0.2250		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.7950		KDB
ΔcH°liquid	[-1240.30; -1215.70]	kJ/mol
ΔcH°liquid	-1240.30 ± 1.60	kJ/mol	NIST
ΔcH°liquid	-1215.70	kJ/mol	NIST
μ	1.00	debye	KDB
η	0.0017330	Pa×s	Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
ΔfG°	-10.60	kJ/mol	KDB
ΔfH°gas	[-38.94; -37.60]	kJ/mol
ΔfH°gas	-37.60 ± 1.30	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-38.94	kJ/mol	KDB
ΔfusH°	11.51	kJ/mol	Joback Calculated Property
ΔvapH°	[23.70; 42.40]	kJ/mol
ΔvapH°	41.74	kJ/mol	NIST
ΔvapH°	41.70 ± 0.80	kJ/mol	NIST
ΔvapH°	42.40	kJ/mol	NIST
ΔvapH°	41.70 ± 0.80	kJ/mol	NIST
ΔvapH°	41.80	kJ/mol	NIST
ΔvapH°	41.73 ± 0.02	kJ/mol	NIST
ΔvapH°	Outlier 23.70 ± 0.20	kJ/mol	NIST
IE	[10.20; 10.58]	eV
IE	10.35 ± 0.04	eV	NIST
IE	10.37	eV	NIST
IE	10.42	eV	NIST
IE	10.20	eV	NIST
IE	10.38	eV	NIST
IE	10.37	eV	NIST
IE	10.58 ± 0.10	eV	NIST
IE	10.44 ± 0.10	eV	NIST
IE	10.57 ± 0.02	eV	NIST
log10WS	[-1.68; -1.68]
log10WS	-1.68		Aq. Solubility Prediction
log10WS	-1.68		Estimated Solubility
logPoct/wat	1.776		Crippen Calculated Property
McVol	74.040	ml/mol	McGowan Calculated Property
Pc	[5335.77; 7200.00]	kPa
Pc	5335.77	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	7200.00	kPa	KDB
Inp	[770.90; 827.00]
Inp	795.00		NIST
Inp	805.00		NIST
Inp	787.00		NIST
Inp	791.00		NIST
Inp	783.90		NIST
Inp	783.00		NIST
Inp	770.90		NIST
Inp	803.00		NIST
Inp	805.00		NIST
Inp	811.00		NIST
Inp	787.00		NIST
Inp	774.00		NIST
Inp	790.00		NIST
Inp	827.00		NIST
Inp	790.00		NIST
Inp	823.00		NIST
Inp	814.90		NIST
Ip	[1226.00; 1299.71]
Ip	1247.00		NIST
Ip	1265.00		NIST
Ip	1286.00		NIST
Ip	1299.71		NIST
Ip	1267.79		NIST
Ip	1226.00		NIST
Ip	1265.00		NIST
Ip	1247.00		NIST
S°liquid	223.30	J/mol×K	NIST
Tboil	[323.70; 464.39]	K
Tboil	404.65	K	Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
Tboil	404.70	K	KDB
Tboil	404.50	K	NIST
Tboil	404.80	K	NIST
Tboil	402.65 ± 0.60	K	NIST
Tboil	404.00 ± 2.00	K	NIST
Tboil	402.00 ± 3.00	K	NIST
Tboil	405.00 ± 3.00	K	NIST
Tboil	398.00 ± 20.00	K	NIST
Tboil	404.90 ± 0.80	K	NIST
Tboil	404.90 ± 1.00	K	NIST
Tboil	402.65 ± 1.50	K	NIST
Tboil	404.30 ± 0.60	K	NIST
Tboil	404.56 ± 0.07	K	NIST
Tboil	403.70 ± 1.50	K	NIST
Tboil	404.80 ± 0.50	K	NIST
Tboil	385.70 ± 20.00	K	NIST
Tboil	404.80 ± 0.30	K	NIST
Tboil	404.90 ± 1.00	K	NIST
Tboil	404.90 ± 1.00	K	NIST
Tboil	404.80 ± 0.40	K	NIST
Tboil	404.80 ± 0.50	K	NIST
Tboil	Outlier 464.39 ± 0.20	K	NIST
Tboil	404.80 ± 0.50	K	NIST
Tboil	404.80 ± 0.40	K	NIST
Tboil	404.80 ± 0.50	K	NIST
Tboil	404.60 ± 0.50	K	NIST
Tboil	404.85 ± 0.30	K	NIST
Tboil	404.85 ± 0.30	K	NIST
Tboil	403.00 ± 2.00	K	NIST
Tboil	404.80 ± 0.30	K	NIST
Tboil	404.45 ± 0.40	K	NIST
Tboil	405.80 ± 0.80	K	NIST
Tboil	404.30 ± 0.50	K	NIST
Tboil	Outlier 323.70 ± 1.00	K	NIST
Tboil	404.20 ± 1.50	K	NIST
Tboil	402.00 ± 1.50	K	NIST
Tboil	404.70 ± 1.50	K	NIST
Tboil	402.15 ± 1.50	K	NIST
Tc	[583.00; 646.00]	K
Tc	646.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	583.00	K	KDB
Tfus	[282.35; 283.20]	K
Tfus	283.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	283.08	K	KDB
Tfus	283.12	K	Aq. Solubility Prediction
Tfus	283.00 ± 0.02	K	NIST
Tfus	282.80 ± 0.30	K	NIST
Tfus	283.20 ± 2.00	K	NIST
Tfus	283.02 ± 0.05	K	NIST
Tfus	283.08 ± 0.10	K	NIST
Tfus	282.85 ± 0.20	K	NIST
Tfus	282.85 ± 0.20	K	NIST
Tfus	283.00 ± 0.05	K	NIST
Tfus	Outlier 282.35 ± 0.50	K	NIST
Ttriple	[282.90; 283.00]	K
Ttriple	282.90	K	KDB
Ttriple	283.00 ± 0.20	K	NIST
Ttriple	283.00 ± 0.20	K	NIST
Vc	0.252	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[129.50; 140.91]	J/mol×K	[285.15; 398.00]
Cp,liquid	136.31	J/mol×K	285.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	136.37	J/mol×K	286.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	136.43	J/mol×K	288.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	136.50	J/mol×K	289.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	135.70	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	136.56	J/mol×K	291.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	136.63	J/mol×K	292.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	134.80	J/mol×K	293.00	NIST
Cp,liquid	136.87	J/mol×K	293.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	136.70	J/mol×K	294.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	136.90	J/mol×K	294.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	136.95	J/mol×K	295.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	136.77	J/mol×K	295.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	136.99	J/mol×K	296.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.02	J/mol×K	297.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	136.84	J/mol×K	297.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	135.00	J/mol×K	298.15	NIST
Cp,liquid	135.60	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	136.00	J/mol×K	298.15	NIST
Cp,liquid	137.04	J/mol×K	298.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	136.89	J/mol×K	298.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	134.70	J/mol×K	298.15	NIST
Cp,liquid	136.92	J/mol×K	298.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.09	J/mol×K	299.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	129.50	J/mol×K	300.00	NIST
Cp,liquid	136.40	J/mol×K	300.00	NIST
Cp,liquid	135.60	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	137.11	J/mol×K	300.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	136.99	J/mol×K	300.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.15	J/mol×K	301.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.07	J/mol×K	301.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.20	J/mol×K	302.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.25	J/mol×K	303.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.15	J/mol×K	303.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.29	J/mol×K	304.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.23	J/mol×K	304.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.32	J/mol×K	305.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.31	J/mol×K	306.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.39	J/mol×K	306.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.42	J/mol×K	307.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.39	J/mol×K	307.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.49	J/mol×K	308.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.48	J/mol×K	309.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.53	J/mol×K	309.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	135.14	J/mol×K	310.00	NIST
Cp,liquid	136.00	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	137.60	J/mol×K	310.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.57	J/mol×K	310.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.65	J/mol×K	311.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.66	J/mol×K	312.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.71	J/mol×K	312.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.77	J/mol×K	313.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	137.75	J/mol×K	313.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.84	J/mol×K	315.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.93	J/mol×K	316.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.03	J/mol×K	318.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.13	J/mol×K	319.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	137.00	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	138.22	J/mol×K	321.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.33	J/mol×K	322.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.43	J/mol×K	324.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.53	J/mol×K	325.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.64	J/mol×K	327.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.74	J/mol×K	328.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.85	J/mol×K	330.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	138.96	J/mol×K	331.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.07	J/mol×K	333.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.19	J/mol×K	334.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.30	J/mol×K	336.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.42	J/mol×K	337.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.54	J/mol×K	339.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.66	J/mol×K	340.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.78	J/mol×K	342.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	139.90	J/mol×K	343.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.03	J/mol×K	345.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.16	J/mol×K	346.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.29	J/mol×K	348.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.42	J/mol×K	349.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.55	J/mol×K	351.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.68	J/mol×K	352.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.82	J/mol×K	354.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	140.91	J/mol×K	355.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	134.70	J/mol×K	398.00	NIST
ΔfusH	[1.94; 10.94]	kJ/mol	[249.50; 283.00]
ΔfusH	1.94	kJ/mol	249.50	NIST
ΔfusH	10.94	kJ/mol	283.00	NIST
ΔsubH	[49.80; 54.80]	kJ/mol	[238.50; 266.00]
ΔsubH	54.80	kJ/mol	238.50	NIST
ΔsubH	49.80	kJ/mol	266.00	NIST
ΔvapH	[31.10; 49.60]	kJ/mol	[291.50; 491.00]
ΔvapH	49.60	kJ/mol	291.50	NIST
ΔvapH	41.80	kJ/mol	300.00	NIST
ΔvapH	41.70 ± 0.10	kJ/mol	308.00	NIST
ΔvapH	41.70 ± 0.10	kJ/mol	315.00	NIST
ΔvapH	41.60 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	31.10	kJ/mol	325.00	NIST
ΔvapH	41.50 ± 0.10	kJ/mol	330.00	NIST
ΔvapH	41.40 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	39.60	kJ/mol	364.50	NIST
ΔvapH	40.00	kJ/mol	402.00	NIST
ΔvapH	36.36	kJ/mol	404.60	KDB
ΔvapH	41.78	kJ/mol	404.70	NIST
ΔvapH	34.77	kJ/mol	404.80	NIST
ΔvapH	37.40	kJ/mol	491.00	NIST
n0	1.53570		298.15	Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
ρl	[2179.24; 2180.01]	kg/m3	[293.00; 293.20]
ρl	2180.01	kg/m3	293.00	KDB
ρl	2179.60	kg/m3	293.15	Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
ρl	2179.24	kg/m3	293.20	Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
ρl	2179.24	kg/m3	293.20	Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
ΔfusS	[7.78; 38.66]	J/mol×K	[249.50; 283.00]
ΔfusS	7.78	J/mol×K	249.50	NIST
ΔfusS	38.66	J/mol×K	283.00	NIST
csound,fluid	[994.27; 1007.04]	m/s	[293.15; 298.15]
csound,fluid	1007.04	m/s	293.15	Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
csound,fluid	994.27	m/s	298.15	Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
γ	[0.04; 0.04]	N/m	[293.15; 313.15]
γ	0.04	N/m	293.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	293.20	KDB
γ	0.04	N/m	298.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	303.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	308.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	313.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[75.88; 140.65]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.74520e+01
Coefficient B			2.70200e-01
Coefficient C			-2.27800e-04
Coefficient D			8.08000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	75.88	J/mol×K	273.00	Calculated Property
Cp,gas	88.11	J/mol×K	353.78	Calculated Property
Cp,gas	98.48	J/mol×K	434.56	Calculated Property
Cp,gas	107.26	J/mol×K	515.33	Calculated Property
Cp,gas	114.69	J/mol×K	596.11	Calculated Property
Cp,gas	121.03	J/mol×K	676.89	Calculated Property
Cp,gas	126.55	J/mol×K	757.67	Calculated Property
Cp,gas	131.48	J/mol×K	838.44	Calculated Property
Cp,gas	136.10	J/mol×K	919.22	Calculated Property
Cp,gas	140.65	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.76; 5624.74]	kPa	[282.94; 650.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46602e+01
Coefficient B			-3.70799e+03
Coefficient C			-3.47480e+01
Temperature range, min.			282.94
Temperature range, max.			650.15
Pvap	0.76	kPa	282.94	Calculated Property
Pvap	6.23	kPa	323.74	Calculated Property
Pvap	30.47	kPa	364.54	Calculated Property
Pvap	105.08	kPa	405.34	Calculated Property
Pvap	283.46	kPa	446.14	Calculated Property
Pvap	639.26	kPa	486.95	Calculated Property
Pvap	1260.10	kPa	527.75	Calculated Property
Pvap	2239.12	kPa	568.55	Calculated Property
Pvap	3666.84	kPa	609.35	Calculated Property
Pvap	5624.74	kPa	650.15	Calculated Property
Pvap	[0.75; 5365.44]	kPa	[282.94; 650.15]	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			3.51685e+01
Coefficient B			-5.52047e+03
Coefficient C			-2.83216e+00
Coefficient D			6.02747e-07
Coefficient E			0.00000e+00
Temperature range, min.			282.94
Temperature range, max.			650.15
Pvap	0.75	kPa	282.94	Calculated Property
Pvap	6.11	kPa	323.74	Calculated Property
Pvap	29.94	kPa	364.54	Calculated Property
Pvap	103.74	kPa	405.34	Calculated Property
Pvap	280.55	kPa	446.14	Calculated Property
Pvap	631.85	kPa	486.95	Calculated Property
Pvap	1239.17	kPa	527.75	Calculated Property
Pvap	2184.04	kPa	568.55	Calculated Property
Pvap	3539.60	kPa	609.35	Calculated Property
Pvap	5365.44	kPa	650.15	Calculated Property
Pvap	[0.12; 103.73]	kPa	[246.00; 404.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			2.15732e+01
Coefficient B			-9.44324e+03
Coefficient C			1.53034e+02
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			246.00
Temperature range, max.			404.70
Pvap	0.12	kPa	246.00	Calculated Property
Pvap	0.34	kPa	263.63	Calculated Property
Pvap	0.84	kPa	281.27	Calculated Property
Pvap	1.97	kPa	298.90	Calculated Property
Pvap	4.32	kPa	316.53	Calculated Property
Pvap	8.94	kPa	334.17	Calculated Property
Pvap	17.59	kPa	351.80	Calculated Property
Pvap	33.08	kPa	369.43	Calculated Property
Pvap	59.68	kPa	387.07	Calculated Property
Pvap	103.73	kPa	404.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.03]	N/m	[283.15; 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			7.89058e-02
Coefficient B			-1.32000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			283.15
Temperature range, max.			404.85
γ	0.04	N/m	283.15	Calculated Property
γ	0.04	N/m	296.67	Calculated Property
γ	0.04	N/m	310.19	Calculated Property
γ	0.04	N/m	323.72	Calculated Property
γ	0.03	N/m	337.24	Calculated Property
γ	0.03	N/m	350.76	Calculated Property
γ	0.03	N/m	364.28	Calculated Property
γ	0.03	N/m	377.81	Calculated Property
γ	0.03	N/m	391.33	Calculated Property
γ	0.03	N/m	404.85	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, 1,2-dibromo-.

Mixtures

• Formic acid, butyl ester + Ethane, 1,2-dibromo-
• Ethane, 1,2-dibromo- + Acetic acid, butyl ester
• Propanoic acid, butyl ester + Ethane, 1,2-dibromo-
• Butanoic acid, butyl ester + Ethane, 1,2-dibromo-
• Ethyl formate + Ethane, 1,2-dibromo-
• Ethane, 1,2-dibromo- + Ethyl Acetate
• Propanoic acid, ethyl ester + Ethane, 1,2-dibromo-
• Ethane, 1,2-dibromo- + Butanoic acid, ethyl ester
• Pentanoic acid, ethyl ester + Ethane, 1,2-dibromo-
• Ethane, 1,2-dibromo- + 1-Hexanol
• Ethane, 1,2-dibromo- + Ethane, 1,2-dichloro-
• Trichloromethane + Ethane, 1,2-dibromo-
• Ethane, 1,2-dibromo- + Ethane, 1,1,2,2-tetrachloro-
• Ethane, 1,2-dibromo- + Methyl formate
• Ethane, 1,2-dibromo- + Acetic acid, methyl ester
• Ethane, 1,2-dibromo- + Methyl propionate
• Butanoic acid, methyl ester + Ethane, 1,2-dibromo-
• Ethane, 1,2-dibromo- + Methyl valerate
• Ethane, 1,2-dibromo- + 1-Decanol
• Ethane, 1,1,1-trichloro- + Ethane, 1,2-dibromo-

Find more mixtures with Ethane, 1,2-dibromo-.

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).
• 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.
• Crippen Method
• Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
• Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
• Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
• Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
• Thermodynamic study of (alkyl esters + alpha,beta-alkyl dihalides) VI.H and V for 20 binary mixtures {xCu-1H2u-1CO2(CH2)3CH3 + (1 - x)alpha,omega-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, alpha = 1, and v = omega = 2 to 6
• Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
• The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
• Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
• Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
• Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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