Chemical Properties of Biphenyl (CAS 92-52-4)

InChI

InChI=1S/C12H10/c1-3-7-11(8-4-1)12-9-5-2-6-10-12/h1-10H

InChI Key

ZUOUZKKEUPVFJK-UHFFFAOYSA-N

Formula

C12H10

SMILES

c1ccc(-c2ccccc2)cc1

Molecular Weight¹

154.21

CAS

92-52-4

Other Names

• 1,1'-Diphenyl
• 1,1'-biphenyl
• 1,1-Biphenyl
• Bibenzene
• Carolid AL
• Lemonene
• NSC 14916
• PhPh
• Phenador-X
• Tetrosin LY
• Xenene
• diphenyl
• phenylbenzene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_solid : Standard solid 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).
• 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°_solid : Solid 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_subH° : Enthalpy of sublimation at standard conditions (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).
• 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).
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• Δ_subS : Entropy of sublimation at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : 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).
• v_spec : Specific Volume (m³/kg).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3643; 0.3720]
ω	0.3643		ChemSep v8.3 pure component data
ω	0.3720		KDB
PAff	[808.80; 813.60]	kJ/mol
PAff	813.60	kJ/mol	NIST
PAff	808.80	kJ/mol	NIST
BasG	[780.70; 782.90]	kJ/mol
BasG	782.90	kJ/mol	NIST
BasG	780.70	kJ/mol	NIST
ΔcH°solid	[-6276.00; -6243.00]	kJ/mol
ΔcH°solid	-6248.00 ± 2.00	kJ/mol	NIST
ΔcH°solid	-6251.80 ± 1.40	kJ/mol	NIST
ΔcH°solid	-6248.20 ± 4.00	kJ/mol	NIST
ΔcH°solid	-6248.50 ± 1.60	kJ/mol	NIST
ΔcH°solid	-6248.80 ± 6.30	kJ/mol	NIST
ΔcH°solid	-6243.00	kJ/mol	NIST
ΔcH°solid	Outlier -6276.00	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data
EA	0.13 ± 0.04	eV	NIST
ΔfG°	[280.08; 280.30]	kJ/mol
ΔfG°	280.08	kJ/mol	ChemSep v8.3 pure component data
ΔfG°	280.30	kJ/mol	KDB
ΔfH°gas	[178.40; 182.20]	kJ/mol
ΔfH°gas	182.09	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	182.20	kJ/mol	KDB
ΔfH°gas	180.30 ± 3.30	kJ/mol	NIST
ΔfH°gas	182.00 ± 0.70	kJ/mol	NIST
ΔfH°gas	181.10 ± 1.80	kJ/mol	NIST
ΔfH°gas	182.10 ± 2.60	kJ/mol	NIST
ΔfH°gas	178.40	kJ/mol	NIST
ΔfH°gas	178.80	kJ/mol	NIST
ΔfH°solid	[96.70; 100.50]	kJ/mol
ΔfH°solid	98.20 ± 2.50	kJ/mol	NIST
ΔfH°solid	96.70 ± 2.60	kJ/mol	NIST
ΔfH°solid	100.50 ± 1.50	kJ/mol	NIST
ΔfH°solid	96.80 ± 4.00	kJ/mol	NIST
ΔfH°solid	97.20 ± 1.60	kJ/mol	NIST
ΔfusH°	19.30	kJ/mol	Synthesis and characterization of novel binary organic monotectic and eutectic alloys
ΔsubH°	[77.90; 84.40]	kJ/mol
ΔsubH°	82.10 ± 2.10	kJ/mol	NIST
ΔsubH°	82.90	kJ/mol	NIST
ΔsubH°	81.52 ± 0.16	kJ/mol	NIST
ΔsubH°	81.50 ± 0.20	kJ/mol	NIST
ΔsubH°	Outlier 77.90 ± 0.30	kJ/mol	NIST
ΔsubH°	81.80 ± 0.20	kJ/mol	NIST
ΔsubH°	84.40	kJ/mol	NIST
ΔsubH°	81.80 ± 0.20	kJ/mol	NIST
ΔsubH°	81.80 ± 0.40	kJ/mol	NIST
ΔsubH°	81.60	kJ/mol	NIST
ΔvapH°	[47.95; 66.20]	kJ/mol
ΔvapH°	65.00	kJ/mol	NIST
ΔvapH°	62.50	kJ/mol	NIST
ΔvapH°	64.50 ± 2.20	kJ/mol	NIST
ΔvapH°	66.20	kJ/mol	NIST
ΔvapH°	66.00	kJ/mol	NIST
ΔvapH°	64.90	kJ/mol	NIST
ΔvapH°	Outlier 47.95	kJ/mol	NIST
IE	[7.95; 8.90]	eV
IE	8.16 ± 0.13	eV	NIST
IE	8.80 ± 0.05	eV	NIST
IE	Outlier 8.90	eV	NIST
IE	7.95 ± 0.02	eV	NIST
IE	8.23 ± 0.01	eV	NIST
IE	8.20 ± 0.05	eV	NIST
IE	8.46	eV	NIST
IE	8.22 ± 0.15	eV	NIST
IE	8.27 ± 0.01	eV	NIST
IE	8.64	eV	NIST
IE	8.35	eV	NIST
IE	8.40	eV	NIST
IE	8.39	eV	NIST
IE	8.34	eV	NIST
log10WS	[-4.38; -4.34]
log10WS	-4.38		Aq. Solubility Prediction
log10WS	-4.34		Estimated Solubility
logPoct/wat	3.354		Crippen Calculated Property
McVol	132.420	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
NFPA Health	2		KDB
Pc	[3120.00; 4084.00]	kPa
Pc	3847.27	kPa	ChemSep v8.3 pure component data
Pc	3380.00	kPa	KDB
Pc	3400.00 ± 100.00	kPa	NIST
Pc	3346.00 ± 103.42	kPa	NIST
Pc	3500.00 ± 101.33	kPa	NIST
Pc	3800.00 ± 689.50	kPa	NIST
Pc	3120.00 ± 202.65	kPa	NIST
Pc	4084.00 ± 137.89	kPa	NIST
Pc	3218.08 ± 81.06	kPa	NIST
Pc	3226.19 ± 81.06	kPa	NIST
Ptriple	0.08	kPa	ChemSep v8.3 pure component data
ρc	[306.87; 322.29]	kg/m3
ρc	308.42 ± 15.42	kg/m3	NIST
ρc	309.96 ± 10.02	kg/m3	NIST
ρc	322.29 ± 10.02	kg/m3	NIST
ρc	306.87 ± 14.96	kg/m3	NIST
Inp	[229.21; 1408.00]
Inp	1369.00		NIST
Inp	1369.00		NIST
Inp	1370.00		NIST
Inp	1378.00		NIST
Inp	1353.00		NIST
Inp	1340.00		NIST
Inp	1340.00		NIST
Inp	1382.00		NIST
Inp	1351.00		NIST
Inp	1351.00		NIST
Inp	1351.00		NIST
Inp	1352.00		NIST
Inp	1352.00		NIST
Inp	1352.00		NIST
Inp	1352.00		NIST
Inp	1352.00		NIST
Inp	1352.00		NIST
Inp	1352.00		NIST
Inp	1354.00		NIST
Inp	1387.00		NIST
Inp	1359.00		NIST
Inp	1366.30		NIST
Inp	1377.90		NIST
Inp	1396.00		NIST
Inp	1373.00		NIST
Inp	1405.00		NIST
Inp	1398.70		NIST
Inp	1354.00		NIST
Inp	1380.00		NIST
Inp	1399.00		NIST
Inp	1354.00		NIST
Inp	1345.00		NIST
Inp	1346.00		NIST
Inp	1349.00		NIST
Inp	1350.00		NIST
Inp	1389.00		NIST
Inp	1377.30		NIST
Inp	1375.40		NIST
Inp	1368.50		NIST
Inp	1377.30		NIST
Inp	1381.80		NIST
Inp	1338.40		NIST
Inp	1392.20		NIST
Inp	1387.00		NIST
Inp	1368.50		NIST
Inp	1377.30		NIST
Inp	1381.80		NIST
Inp	1375.40		NIST
Inp	1381.00		NIST
Inp	1375.78		NIST
Inp	1377.20		NIST
Inp	1377.91		NIST
Inp	1396.81		NIST
Inp	1392.00		NIST
Inp	1392.64		NIST
Inp	1390.72		NIST
Inp	1384.00		NIST
Inp	1374.00		NIST
Inp	1378.00		NIST
Inp	1349.00		NIST
Inp	1350.00		NIST
Inp	1364.00		NIST
Inp	1373.00		NIST
Inp	1362.00		NIST
Inp	1397.00		NIST
Inp	1371.00		NIST
Inp	1375.00		NIST
Inp	1366.00		NIST
Inp	1360.00		NIST
Inp	1360.00		NIST
Inp	1408.00		NIST
Inp	1368.00		NIST
Inp	1396.00		NIST
Inp	1384.00		NIST
Inp	1385.30		NIST
Inp	1379.00		NIST
Inp	1388.00		NIST
Inp	1380.00		NIST
Inp	1380.00		NIST
Inp	1381.00		NIST
Inp	1381.00		NIST
Inp	1381.00		NIST
Inp	1382.00		NIST
Inp	1385.00		NIST
Inp	1385.00		NIST
Inp	1354.00		NIST
Inp	1356.00		NIST
Inp	1356.00		NIST
Inp	1342.00		NIST
Inp	1358.00		NIST
Inp	1366.00		NIST
Inp	1345.00		NIST
Inp	1380.00		NIST
Inp	1391.00		NIST
Inp	1385.00		NIST
Inp	1394.00		NIST
Inp	1369.00		NIST
Inp	1375.00		NIST
Inp	1356.00		NIST
Inp	1384.00		NIST
Inp	1384.00		NIST
Inp	1368.00		NIST
Inp	1369.00		NIST
Inp	1362.00		NIST
Inp	1362.00		NIST
Inp	1348.00		NIST
Inp	1342.00		NIST
Inp	1343.00		NIST
Inp	1349.00		NIST
Inp	1350.00		NIST
Inp	1389.00		NIST
Inp	1389.00		NIST
Inp	245.80		NIST
Inp	237.70		NIST
Inp	236.39		NIST
Inp	236.39		NIST
Inp	236.34		NIST
Inp	235.88		NIST
Inp	236.15		NIST
Inp	236.19		NIST
Inp	236.26		NIST
Inp	236.32		NIST
Inp	236.87		NIST
Inp	236.92		NIST
Inp	237.02		NIST
Inp	237.04		NIST
Inp	236.28		NIST
Inp	236.48		NIST
Inp	231.10		NIST
Inp	235.60		NIST
Inp	233.57		NIST
Inp	234.13		NIST
Inp	235.55		NIST
Inp	233.78		NIST
Inp	233.46		NIST
Inp	236.40		NIST
Inp	236.20		NIST
Inp	236.00		NIST
Inp	235.63		NIST
Inp	232.74		NIST
Inp	236.39		NIST
Inp	233.96		NIST
Inp	236.59		NIST
Inp	234.05		NIST
Inp	230.79		NIST
Inp	229.80		NIST
Inp	236.44		NIST
Inp	233.96		NIST
Inp	236.60		NIST
Inp	236.56		NIST
Inp	236.39		NIST
Inp	236.56		NIST
Inp	235.50		NIST
Inp	240.35		NIST
Inp	229.33		NIST
Inp	235.00		NIST
Inp	235.00		NIST
Inp	229.21		NIST
Inp	235.74		NIST
Inp	233.96		NIST
Inp	233.96		NIST
Inp	235.51		NIST
Inp	237.30		NIST
Inp	235.60		NIST
Inp	236.40		NIST
Inp	232.86		NIST
Inp	232.96		NIST
Inp	236.20		NIST
Inp	233.96		NIST
Inp	1377.30		NIST
Inp	1338.40		NIST
Inp	1381.80		NIST
Inp	1377.91		NIST
Inp	1384.00		NIST
Inp	1364.00		NIST
Inp	245.80		NIST
Inp	235.88		NIST
Inp	236.87		NIST
Inp	236.48		NIST
Inp	235.55		NIST
Inp	236.00		NIST
Inp	236.59		NIST
Inp	233.96		NIST
I	[228.73; 2030.00]
I	2029.00		NIST
I	1996.00		NIST
I	2016.00		NIST
I	1996.00		NIST
I	2030.00		NIST
I	1981.00		NIST
I	1967.00		NIST
I	2012.00		NIST
I	1981.00		NIST
I	1974.00		NIST
I	1974.00		NIST
I	1981.00		NIST
I	Outlier 228.73		NIST
I	2030.00		NIST
I	2029.00		NIST
I	Outlier 228.73		NIST
I	2012.00		NIST
S°solid,1 bar	[205.90; 209.38]	J/mol×K
S°solid,1 bar	209.38	J/mol×K	NIST
S°solid,1 bar	209.00	J/mol×K	NIST
S°solid,1 bar	205.90	J/mol×K	NIST
Tboil	[518.00; 538.25]	K
Tboil	528.15	K	ChemSep v8.3 pure component data
Tboil	529.20	K	KDB
Tboil	529.10	K	NIST
Tboil	527.50 ± 0.50	K	NIST
Tboil	Outlier 538.25 ± 0.60	K	NIST
Tboil	Outlier 518.00 ± 5.00	K	NIST
Tboil	527.00 ± 2.00	K	NIST
Tboil	528.00 ± 3.00	K	NIST
Tboil	529.25 ± 0.50	K	NIST
Tboil	527.00 ± 3.00	K	NIST
Tboil	529.25 ± 0.30	K	NIST
Tboil	529.25 ± 0.40	K	NIST
Tboil	528.00 ± 2.00	K	NIST
Tboil	528.00 ± 3.00	K	NIST
Tboil	527.00 ± 3.00	K	NIST
Tboil	528.40 ± 1.11	K	NIST
Tboil	525.00 ± 4.00	K	NIST
Tboil	529.10 ± 1.50	K	NIST
Tboil	524.00 ± 4.00	K	NIST
Tboil	527.00 ± 3.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	528.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	525.00 ± 5.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	527.00 ± 4.00	K	NIST
Tboil	525.00 ± 10.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	528.00 ± 7.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tboil	527.00 ± 5.00	K	NIST
Tc	[768.75; 800.00]	K
Tc	780.00	K	ChemSep v8.3 pure component data
Tc	773.00	K	KDB
Tc	773.00 ± 3.00	K	NIST
Tc	773.00 ± 3.00	K	NIST
Tc	777.00 ± 6.00	K	NIST
Tc	789.00 ± 5.60	K	NIST
Tc	769.00 ± 3.00	K	NIST
Tc	Outlier 800.00 ± 11.11	K	NIST
Tc	768.75 ± 2.00	K	NIST
Tfus	[314.30; 350.00]	K
Tfus	341.10	K	Solid-liquid equilibria of eicosane, tetracosane or biphenyl + 1- octadecanol, or + 1-eicosanol mixtures
Tfus	342.10	K	The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters
Tfus	342.08	K	Investigation of the melting behavior of the reference materials biphenyl and phenyl salicylate by a new type adiabatic scanning calorimeter
Tfus	342.35	K	ChemSep v8.3 pure component data
Tfus	342.00	K	KDB
Tfus	342.84	K	Aq. Solubility Prediction
Tfus	342.41 ± 0.05	K	NIST
Tfus	342.35 ± 0.50	K	NIST
Tfus	342.60 ± 0.20	K	NIST
Tfus	341.99 ± 0.10	K	NIST
Tfus	342.20 ± 1.00	K	NIST
Tfus	344.00	K	NIST
Tfus	343.30 ± 0.20	K	NIST
Tfus	342.20 ± 0.30	K	NIST
Tfus	344.10 ± 0.20	K	NIST
Tfus	342.00 ± 0.20	K	NIST
Tfus	342.20 ± 0.20	K	NIST
Tfus	342.10 ± 0.10	K	NIST
Tfus	344.00 ± 2.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	Outlier 332.00 ± 4.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	342.11 ± 0.02	K	NIST
Tfus	342.12 ± 0.01	K	NIST
Tfus	342.20 ± 2.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	342.60 ± 2.00	K	NIST
Tfus	340.00 ± 4.00	K	NIST
Tfus	343.20 ± 0.30	K	NIST
Tfus	342.11 ± 0.02	K	NIST
Tfus	342.11 ± 0.02	K	NIST
Tfus	342.12 ± 0.01	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.40 ± 1.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.20 ± 2.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.40 ± 0.50	K	NIST
Tfus	343.00 ± 1.50	K	NIST
Tfus	343.50 ± 0.50	K	NIST
Tfus	341.00 ± 3.00	K	NIST
Tfus	344.00 ± 2.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	344.30 ± 1.00	K	NIST
Tfus	342.00 ± 4.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	343.00 ± 1.50	K	NIST
Tfus	342.20 ± 2.00	K	NIST
Tfus	342.00 ± 4.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	342.40 ± 0.70	K	NIST
Tfus	342.30 ± 0.15	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	342.70 ± 1.50	K	NIST
Tfus	343.00 ± 0.50	K	NIST
Tfus	342.65 ± 1.50	K	NIST
Tfus	344.00 ± 1.50	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	342.70 ± 1.50	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	342.60 ± 1.50	K	NIST
Tfus	342.20 ± 1.50	K	NIST
Tfus	342.00 ± 1.50	K	NIST
Tfus	341.00 ± 2.00	K	NIST
Tfus	342.03 ± 0.06	K	NIST
Tfus	342.03 ± 0.05	K	NIST
Tfus	342.00 ± 0.30	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	344.00 ± 2.00	K	NIST
Tfus	342.10 ± 2.50	K	NIST
Tfus	340.00 ± 3.00	K	NIST
Tfus	339.00 ± 2.00	K	NIST
Tfus	344.00 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	340.00 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	339.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	342.70 ± 2.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	342.40 ± 0.15	K	NIST
Tfus	342.40 ± 0.50	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	342.40 ± 1.00	K	NIST
Tfus	341.70 ± 0.50	K	NIST
Tfus	342.70 ± 2.00	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	345.00 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.70 ± 2.00	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	341.70 ± 2.00	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	342.30 ± 0.80	K	NIST
Tfus	342.30 ± 0.70	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	343.40 ± 1.00	K	NIST
Tfus	343.30 ± 0.50	K	NIST
Tfus	342.70 ± 2.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	342.10 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	344.00 ± 1.00	K	NIST
Tfus	344.00 ± 1.00	K	NIST
Tfus	344.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.40 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	341.00 ± 2.00	K	NIST
Tfus	342.20 ± 0.30	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	344.00 ± 1.00	K	NIST
Tfus	342.30 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	341.70 ± 2.00	K	NIST
Tfus	342.00 ± 1.00	K	NIST
Tfus	342.70 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	341.50 ± 0.20	K	NIST
Tfus	342.70 ± 2.00	K	NIST
Tfus	342.00 ± 1.50	K	NIST
Tfus	342.40 ± 1.11	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.60 ± 1.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	342.70 ± 1.00	K	NIST
Tfus	342.40 ± 0.55	K	NIST
Tfus	342.30 ± 0.70	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.40 ± 0.40	K	NIST
Tfus	342.40 ± 1.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	341.70 ± 2.00	K	NIST
Tfus	342.70 ± 2.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	344.70 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.00 ± 2.00	K	NIST
Tfus	344.70 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	344.00 ± 1.00	K	NIST
Tfus	342.55 ± 0.20	K	NIST
Tfus	342.60 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	342.70 ± 1.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	342.70 ± 1.00	K	NIST
Tfus	343.00 ± 1.50	K	NIST
Tfus	344.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	341.90 ± 2.00	K	NIST
Tfus	343.70 ± 1.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	342.10 ± 1.50	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	343.19 ± 0.50	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	344.00 ± 2.00	K	NIST
Tfus	344.00 ± 2.00	K	NIST
Tfus	343.00 ± 2.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	342.10 ± 0.30	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	344.00 ± 2.00	K	NIST
Tfus	342.80 ± 1.50	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 0.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	Outlier 332.00 ± 4.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	343.00 ± 1.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.90 ± 1.50	K	NIST
Tfus	344.00 ± 1.50	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	342.70 ± 2.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	342.20 ± 2.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	343.90 ± 2.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	344.20 ± 2.00	K	NIST
Tfus	344.00 ± 4.00	K	NIST
Tfus	343.70 ± 1.50	K	NIST
Tfus	Outlier 314.30 ± 1.50	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 4.00	K	NIST
Tfus	344.00 ± 3.00	K	NIST
Tfus	344.00 ± 4.00	K	NIST
Tfus	343.00 ± 4.00	K	NIST
Tfus	343.00 ± 4.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	341.00 ± 4.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	343.70 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	344.00 ± 4.00	K	NIST
Tfus	344.00 ± 4.00	K	NIST
Tfus	343.70 ± 3.00	K	NIST
Tfus	344.00 ± 4.00	K	NIST
Tfus	343.70 ± 3.00	K	NIST
Tfus	343.00 ± 4.00	K	NIST
Tfus	343.70 ± 3.00	K	NIST
Tfus	344.00 ± 4.00	K	NIST
Tfus	342.80 ± 3.00	K	NIST
Tfus	344.00 ± 4.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	Outlier 350.00 ± 5.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.70 ± 3.00	K	NIST
Tfus	343.70 ± 3.00	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	342.00 ± 3.00	K	NIST
Tfus	343.70 ± 2.00	K	NIST
Tfus	343.00 ± 3.00	K	NIST
Tfus	343.70 ± 3.00	K	NIST
Ttriple	[341.80; 342.37]	K
Ttriple	342.37	K	ChemSep v8.3 pure component data
Ttriple	342.09 ± 0.01	K	NIST
Ttriple	341.80 ± 0.30	K	NIST
Ttriple	342.09 ± 0.01	K	NIST
UQi	4.24		ChemSep v8.3 pure component data
URi	6.04		ChemSep v8.3 pure component data
Vc	[0.491; 0.497]	m3/kmol
Vc	0.491	m3/kmol	ChemSep v8.3 pure component data
Vc	0.497	m3/kmol	KDB
Vc	0.497	m3/kmol	NIST
Zc	[0.2613710; 0.2940000]
Zc	0.2940000		ChemSep v8.3 pure component data
Zc	0.2613710		KDB
Zra	[0.27; 0.28]
Zra	0.28		ChemSep v8.3 pure component data
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[259.54; 421.70]	J/mol×K	[298.00; 700.00]
Cp,liquid	259.54	J/mol×K	298.00	NIST
Cp,liquid	273.00	J/mol×K	350.00	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	263.20	J/mol×K	350.80	NIST
Cp,liquid	277.30	J/mol×K	360.00	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	285.30	J/mol×K	370.00	NIST
Cp,liquid	281.60	J/mol×K	370.00	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	300.00	J/mol×K	370.00	NIST
Cp,liquid	285.90	J/mol×K	380.00	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	290.20	J/mol×K	390.00	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	294.50	J/mol×K	400.00	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	298.80	J/mol×K	410.00	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	303.10	J/mol×K	420.00	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	301.20	J/mol×K	422.00	NIST
Cp,liquid	307.40	J/mol×K	430.00	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	311.80	J/mol×K	440.00	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	316.10	J/mol×K	450.00	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	320.40	J/mol×K	460.00	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	324.70	J/mol×K	470.00	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	329.00	J/mol×K	480.00	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	333.30	J/mol×K	490.00	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	337.70	J/mol×K	500.00	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	342.00	J/mol×K	510.00	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	346.30	J/mol×K	520.00	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	350.60	J/mol×K	530.00	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	354.80	J/mol×K	540.00	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	359.10	J/mol×K	550.00	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	363.40	J/mol×K	560.00	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	367.70	J/mol×K	570.00	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	371.90	J/mol×K	580.00	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	376.10	J/mol×K	590.00	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	380.40	J/mol×K	600.00	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	384.60	J/mol×K	610.00	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	388.80	J/mol×K	620.00	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	393.00	J/mol×K	630.00	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	397.10	J/mol×K	640.00	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	401.30	J/mol×K	650.00	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	405.40	J/mol×K	660.00	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	409.50	J/mol×K	670.00	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	413.60	J/mol×K	680.00	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	417.70	J/mol×K	690.00	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	421.70	J/mol×K	700.00	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,solid	[190.00; 198.39]	J/mol×K	[294.40; 303.00]
Cp,solid	194.10	J/mol×K	294.40	NIST
Cp,solid	197.90	J/mol×K	298.10	NIST
Cp,solid	198.39	J/mol×K	298.15	NIST
Cp,solid	198.17	J/mol×K	298.15	NIST
Cp,solid	197.70	J/mol×K	298.15	NIST
Cp,solid	190.80	J/mol×K	298.15	NIST
Cp,solid	190.00	J/mol×K	300.00	NIST
Cp,solid	197.90	J/mol×K	303.00	NIST
ΔfusH	[18.57; 19.70]	kJ/mol	[314.30; 344.34]
ΔfusH	18.95	kJ/mol	314.30	NIST
ΔfusH	18.65	kJ/mol	341.50	NIST
ΔfusH	18.66	kJ/mol	341.50	NIST
ΔfusH	18.66	kJ/mol	341.50	NIST
ΔfusH	18.59	kJ/mol	342.00	NIST
ΔfusH	18.58	kJ/mol	342.10	NIST
ΔfusH	18.58	kJ/mol	342.10	NIST
ΔfusH	18.58	kJ/mol	342.20	NIST
ΔfusH	19.70	kJ/mol	342.30	NIST
ΔfusH	18.57	kJ/mol	343.00	NIST
ΔfusH	18.80	kJ/mol	344.10	NIST
ΔfusH	19.27	kJ/mol	344.34	NIST
ΔsubH	[68.60; 83.60]	kJ/mol	[283.00; 383.00]
ΔsubH	83.60 ± 2.50	kJ/mol	283.00	NIST
ΔsubH	81.59	kJ/mol	288.05	NIST
ΔsubH	75.80 ± 0.60	kJ/mol	289.00	NIST
ΔsubH	68.60 ± 0.80	kJ/mol	292.00	NIST
ΔsubH	76.00 ± 4.00	kJ/mol	293.00	NIST
ΔsubH	68.60 ± 0.80	kJ/mol	295.00	NIST
ΔsubH	75.10 ± 1.70	kJ/mol	297.00	NIST
ΔsubH	81.52	kJ/mol	298.15	NIST
ΔsubH	81.52	kJ/mol	298.15	NIST
ΔsubH	81.60 ± 1.70	kJ/mol	301.00	NIST
ΔsubH	75.20	kJ/mol	308.00	NIST
ΔsubH	83.40	kJ/mol	310.50	NIST
ΔsubH	80.40 ± 1.60	kJ/mol	319.00	NIST
ΔsubH	75.81 ± 0.59	kJ/mol	342.50	NIST
ΔsubH	81.80	kJ/mol	383.00	NIST
ΔvapH	[45.61; 64.95]	kJ/mol	[298.00; 647.00]
ΔvapH	64.95	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH	60.40	kJ/mol	363.00	NIST
ΔvapH	59.60	kJ/mol	400.50	NIST
ΔvapH	54.90	kJ/mol	416.50	NIST
ΔvapH	59.40	kJ/mol	443.00	NIST
ΔvapH	60.30	kJ/mol	464.00	NIST
ΔvapH	50.40	kJ/mol	464.00	NIST
ΔvapH	57.40	kJ/mol	464.00	NIST
ΔvapH	57.40	kJ/mol	464.00	NIST
ΔvapH	60.30	kJ/mol	464.00	NIST
ΔvapH	50.40	kJ/mol	464.00	NIST
ΔvapH	57.30	kJ/mol	476.50	NIST
ΔvapH	45.61	kJ/mol	528.20	KDB
ΔvapH	51.20	kJ/mol	591.50	NIST
ΔvapH	48.00	kJ/mol	647.00	NIST
Pvap	[0.10; 0.57]	kPa	[345.70; 376.20]
Pvap	0.10	kPa	345.70	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.12	kPa	347.70	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.12	kPa	348.30	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.14	kPa	350.40	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.16	kPa	353.30	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.22	kPa	358.30	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.28	kPa	363.30	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.35	kPa	368.20	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.37	kPa	368.20	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.48	kPa	373.10	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.54	kPa	375.40	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
Pvap	0.57	kPa	376.20	Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
ρl	990.00	kg/m3	347.00	KDB
ΔfusS	[54.20; 60.30]	J/mol×K	[314.30; 344.10]
ΔfusS	60.30	J/mol×K	314.30	NIST
ΔfusS	54.60	J/mol×K	341.50	NIST
ΔfusS	54.81	J/mol×K	341.50	NIST
ΔfusS	54.40	J/mol×K	342.00	NIST
ΔfusS	54.30	J/mol×K	342.10	NIST
ΔfusS	54.30	J/mol×K	342.10	NIST
ΔfusS	54.30	J/mol×K	342.20	NIST
ΔfusS	54.20	J/mol×K	343.00	NIST
ΔfusS	54.60	J/mol×K	344.10	NIST
γ	0.03	N/m	393.20	KDB
ΔsubS	[273.42; 273.42]	J/mol×K	[298.15; 298.15]
ΔsubS	273.42	J/mol×K	298.15	NIST
ΔsubS	273.42	J/mol×K	298.15	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[347.00; 418.20]	K	[0.03; 2.90]
Tboilr	347.00 ± 4.00	K	0.03	NIST
Tboilr	418.20	K	2.90	NIST
Tboilr	418.00	K	2.90	NIST

Datasets

Specific volume, m3/kg

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Specific volume, m3/kg - Liquid
333.15	100.00	0.0010
343.15	100.00	0.0010
353.15	100.00	0.0010
353.15	10000.00	0.0010
353.15	20000.00	0.0010
353.15	30000.00	0.0010
363.15	100.00	0.0010
363.16	100.00	0.0010
363.16	10000.00	0.0010
363.16	20000.00	0.0010
363.16	30000.00	0.0010
363.16	40000.00	0.0010
363.16	50000.00	0.0010
363.16	60000.00	0.0010
363.16	70000.00	0.0010
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[110.18; 454.75]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			7.95830e+01
Coefficient B			-6.35840e+02
Coefficient C			6.66624e+00
Coefficient D			-3.49350e-04
Coefficient E			9.29100e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	110.18	J/mol×K	200.00	Calculated Property
Cp,gas	190.74	J/mol×K	344.44	Calculated Property
Cp,gas	263.98	J/mol×K	488.89	Calculated Property
Cp,gas	319.02	J/mol×K	633.33	Calculated Property
Cp,gas	359.15	J/mol×K	777.78	Calculated Property
Cp,gas	388.67	J/mol×K	922.22	Calculated Property
Cp,gas	410.95	J/mol×K	1066.67	Calculated Property
Cp,gas	428.35	J/mol×K	1211.11	Calculated Property
Cp,gas	442.56	J/mol×K	1355.56	Calculated Property
Cp,gas	454.75	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[263.86; 401.55]	J/mol×K	[342.20; 623.15]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.41320e+01
Coefficient B			-1.23950e+01
Coefficient C			4.67724e+00
Coefficient D			2.94070e-03
Coefficient E			-1.43310e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			342.20
Temperature range, max.			623.15
Cp,liquid	263.86	J/mol×K	342.20	Calculated Property
Cp,liquid	279.40	J/mol×K	373.42	Calculated Property
Cp,liquid	295.07	J/mol×K	404.63	Calculated Property
Cp,liquid	310.78	J/mol×K	435.85	Calculated Property
Cp,liquid	326.48	J/mol×K	467.07	Calculated Property
Cp,liquid	342.07	J/mol×K	498.28	Calculated Property
Cp,liquid	357.46	J/mol×K	529.50	Calculated Property
Cp,liquid	372.57	J/mol×K	560.72	Calculated Property
Cp,liquid	387.30	J/mol×K	591.93	Calculated Property
Cp,liquid	401.55	J/mol×K	623.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0009487; 0.0001064]	Pa×s	[373.15; 723.15]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.09980e+01
Coefficient B			1.57440e+03
Coefficient C			-2.26710e-02
Coefficient D			-3.40580e-07
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			373.15
Temperature range, max.			723.15
η	0.0009487	Pa×s	373.15	Calculated Property
η	0.0006290	Pa×s	412.04	Calculated Property
η	0.0004464	Pa×s	450.93	Calculated Property
η	0.0003335	Pa×s	489.82	Calculated Property
η	0.0002593	Pa×s	528.71	Calculated Property
η	0.0002081	Pa×s	567.59	Calculated Property
η	0.0001712	Pa×s	606.48	Calculated Property
η	0.0001438	Pa×s	645.37	Calculated Property
η	0.0001228	Pa×s	684.26	Calculated Property
η	0.0001064	Pa×s	723.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[61.10; 0.00]	kJ/mol	[342.37; 780.00]	ChemSep v8.3 pure component data
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			8.68087e+01
Coefficient B			4.73092e-01
Coefficient C			1.06100e+00
Coefficient D			-2.22634e+00
Coefficient E			1.15688e+00
Critical temperature, Tc (K)			7.80000e+02
Comment			ChemSep eq 106, HeatOfVaporization, ChemSep Tmax 789.26 K
Temperature range, min.			342.37
Temperature range, max.			780.00
ΔvapH	61.10	kJ/mol	342.37	Calculated Property
ΔvapH	57.53	kJ/mol	391.00	Calculated Property
ΔvapH	54.07	kJ/mol	439.62	Calculated Property
ΔvapH	50.61	kJ/mol	488.25	Calculated Property
ΔvapH	47.03	kJ/mol	536.87	Calculated Property
ΔvapH	43.09	kJ/mol	585.50	Calculated Property
ΔvapH	38.44	kJ/mol	634.12	Calculated Property
ΔvapH	32.50	kJ/mol	682.75	Calculated Property
ΔvapH	23.93	kJ/mol	731.37	Calculated Property
ΔvapH	0.00	kJ/mol	780.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.09; 4052.27]	kPa	[342.37; 789.26]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.47432e+02
Coefficient B			-1.35554e+04
Coefficient C			-1.90558e+01
Coefficient D			8.30386e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			342.37
Temperature range, max.			789.26
Pvap	0.09	kPa	342.37	Calculated Property
Pvap	1.41	kPa	392.02	Calculated Property
Pvap	9.98	kPa	441.68	Calculated Property
Pvap	42.81	kPa	491.33	Calculated Property
Pvap	131.63	kPa	540.99	Calculated Property
Pvap	323.67	kPa	590.64	Calculated Property
Pvap	684.59	kPa	640.30	Calculated Property
Pvap	1309.83	kPa	689.95	Calculated Property
Pvap	2349.15	kPa	739.61	Calculated Property
Pvap	4052.27	kPa	789.26	Calculated Property
Pvap	[0.11; 3838.88]	kPa	[342.00; 789.26]	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			9.40474e+01
Coefficient B			-1.07952e+04
Coefficient C			-1.11711e+01
Coefficient D			3.86310e-06
Coefficient E			0.00000e+00
Temperature range, min.			342.00
Temperature range, max.			789.26
Pvap	0.11	kPa	342.00	Calculated Property
Pvap	1.47	kPa	391.70	Calculated Property
Pvap	10.09	kPa	441.39	Calculated Property
Pvap	43.55	kPa	491.09	Calculated Property
Pvap	136.35	kPa	540.78	Calculated Property
Pvap	340.48	kPa	590.48	Calculated Property
Pvap	722.79	kPa	640.17	Calculated Property
Pvap	1363.78	kPa	689.87	Calculated Property
Pvap	2361.05	kPa	739.56	Calculated Property
Pvap	3838.88	kPa	789.26	Calculated Property
Pvap	[0.10; 142.04]	kPa	[342.30; 544.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46372e+01
Coefficient B			-4.57667e+03
Coefficient C			-7.15560e+01
Reference			Cunningham, 1930, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			342.30
Temperature range, max.			544.30
Pvap	0.10	kPa	342.30	Calculated Property
Pvap	0.38	kPa	364.74	Calculated Property
Pvap	1.15	kPa	387.19	Calculated Property
Pvap	3.00	kPa	409.63	Calculated Property
Pvap	6.98	kPa	432.08	Calculated Property
Pvap	14.68	kPa	454.52	Calculated Property
Pvap	28.45	kPa	476.97	Calculated Property
Pvap	51.44	kPa	499.41	Calculated Property
Pvap	87.67	kPa	521.86	Calculated Property
Pvap	142.04	kPa	544.30	Calculated Property
Pvap	[0.10; 142.04]	kPa	[342.30; 544.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46372e+01
Coefficient B			-4.57667e+03
Coefficient C			-7.15560e+01
Reference			Cunningham, 1930
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			342.30
Temperature range, max.			544.30
Pvap	0.10	kPa	342.30	Calculated Property
Pvap	0.38	kPa	364.74	Calculated Property
Pvap	1.15	kPa	387.19	Calculated Property
Pvap	3.00	kPa	409.63	Calculated Property
Pvap	6.98	kPa	432.08	Calculated Property
Pvap	14.68	kPa	454.52	Calculated Property
Pvap	28.45	kPa	476.97	Calculated Property
Pvap	51.44	kPa	499.41	Calculated Property
Pvap	87.67	kPa	521.86	Calculated Property
Pvap	142.04	kPa	544.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[991.54; 308.23]	kg/m3	[342.37; 789.26]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.83422e+01
Coefficient B			2.54170e-01
Coefficient C			7.89260e+02
Coefficient D			2.79500e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			342.37
Temperature range, max.			789.26
ρl	991.54	kg/m3	342.37	Calculated Property
ρl	954.72	kg/m3	392.02	Calculated Property
ρl	915.99	kg/m3	441.68	Calculated Property
ρl	874.87	kg/m3	491.33	Calculated Property
ρl	830.68	kg/m3	540.99	Calculated Property
ρl	782.35	kg/m3	590.64	Calculated Property
ρl	728.03	kg/m3	640.30	Calculated Property
ρl	663.98	kg/m3	689.95	Calculated Property
ρl	580.04	kg/m3	739.61	Calculated Property
ρl	308.23	kg/m3	789.26	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 4.24e-06]	N/m	[342.37; 784.34]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-6.95240e-03
Coefficient B			1.42550e+02
Coefficient C			-3.82900e+00
Coefficient D			2.58860e-03
Coefficient E			-5.44730e-06
Comment			ChemSep eq 16, SurfaceTension, ChemSep Tmax 789.26 K
Temperature range, min.			342.37
Temperature range, max.			784.34
γ	0.04	N/m	342.37	Calculated Property
γ	0.03	N/m	391.48	Calculated Property
γ	0.03	N/m	440.59	Calculated Property
γ	0.02	N/m	489.69	Calculated Property
γ	0.02	N/m	538.80	Calculated Property
γ	0.01	N/m	587.91	Calculated Property
γ	0.01	N/m	637.02	Calculated Property
γ	0.01	N/m	686.13	Calculated Property
γ	0.00	N/m	735.24	Calculated Property
γ	4.24e-06	N/m	784.34	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.01; 0.07]	W/m×K	[342.37; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			3.19710e-05
Coefficient B			1.15280e+00
Coefficient C			2.15140e+02
Coefficient D			1.15000e+05
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			342.37
Temperature range, max.			1000.00
λ	0.01	W/m×K	342.37	Calculated Property
λ	0.02	W/m×K	415.44	Calculated Property
λ	0.02	W/m×K	488.51	Calculated Property
λ	0.03	W/m×K	561.58	Calculated Property
λ	0.03	W/m×K	634.65	Calculated Property
λ	0.04	W/m×K	707.72	Calculated Property
λ	0.05	W/m×K	780.79	Calculated Property
λ	0.05	W/m×K	853.86	Calculated Property
λ	0.06	W/m×K	926.93	Calculated Property
λ	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.14; 0.11]	W/m×K	[357.65; 528.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			8.62770e-02
Coefficient B			-3.43480e+02
Coefficient C			3.62610e-01
Coefficient D			-7.91000e-03
Coefficient E			3.25040e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			357.65
Temperature range, max.			528.00
λ	0.14	W/m×K	357.65	Calculated Property
λ	0.13	W/m×K	376.58	Calculated Property
λ	0.13	W/m×K	395.51	Calculated Property
λ	0.13	W/m×K	414.43	Calculated Property
λ	0.13	W/m×K	433.36	Calculated Property
λ	0.12	W/m×K	452.29	Calculated Property
λ	0.12	W/m×K	471.22	Calculated Property
λ	0.12	W/m×K	490.14	Calculated Property
λ	0.12	W/m×K	509.07	Calculated Property
λ	0.11	W/m×K	528.00	Calculated Property

Similar Compounds

Find more compounds similar to Biphenyl.

Mixtures

• Biphenyl + 1-Octadecanol
• Biphenyl + 1-Eicosanol
• 2-Pyrrolidinone, 1-methyl- + Biphenyl
• Biphenyl + Benzaldehyde, 3-hydroxy-
• Carbon dioxide + Biphenyl
• Benzene, 1,1'-oxybis- + Biphenyl
• Biphenyl + Formamide
• Biphenyl + Cyclohexane
• Biphenyl + Heptane
• Benzene + Biphenyl
• Biphenyl + 1,4-Dioxane
• Trichloromethane + Biphenyl
• Carbon dioxide + Biphenyl + Naphthalene
• 1H-INDOLE + Biphenyl
• Biphenyl + Water

Sources

• KDB Vapor Pressure Data
• 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
• PVT Relationships of Binary Mixtures of Indole with 2-Methylnaphthalene and Biphenyl at 333.15 K and Pressures up to 270 MPa
• Enthalpies of solution, partial molar volumes and isentropic compressibilities of polycyclic aromatic hydrocarbons in 1-methyl-2-pyrrolidone at 298.15K
• Solid liquid gas equilibrium of the naphthalene biphenyl CO2 system: Measurement and modeling
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• Solid-liquid equilibria of eicosane, tetracosane or biphenyl + 1- octadecanol, or + 1-eicosanol mixtures
• Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 K
• High-pressure phase diagram of the drug mitotane in compressed and/or supercritical CO2
• Thermophysical properties of diphenyl ether + biphenyl mixtures for their use as heat transfer fluids
• Thermodynamics of solvation and solvophobic effect in formamide
• Isobaric heat capacity at high pressure, density, and viscosity of (diphenyl ether + biphenyl) mixtures
• Benchmark properties of biphenyl as a liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Synthesis and characterization of novel binary organic monotectic and eutectic alloys
• The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters
• Investigation of the melting behavior of the reference materials biphenyl and phenyl salicylate by a new type adiabatic scanning calorimeter
• Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• 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
• The Effects of Temperature and Inorganic Salts on the Aqueous Solubility of Selected Chlorobenzenes
• Solubilities of 4-Phenyltoluene, Phenylboric Acid, Biphenyl, and Iodobenzene in Carbon Dioxide from Measurements of the Relative Permittivity
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• 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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