Chemical Properties of Phenanthrene (CAS 85-01-8)

InChI

InChI=1S/C14H10/c1-3-7-13-11(5-1)9-10-12-6-2-4-8-14(12)13/h1-10H

InChI Key

YNPNZTXNASCQKK-UHFFFAOYSA-N

Formula

C14H10

SMILES

c1ccc2c(c1)ccc1ccccc12

Molecular Weight¹

178.23

CAS

85-01-8

Other Names

• Phenanthren
• Phenanthrin
• Phenantrin

• 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).
• P_c : Critical Pressure (kPa).
• P_sub : Sublimation pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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).
• 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).
• Δ_vapS : Entropy of vaporization 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 : 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	[0.4707; 0.4734]
ω	0.4734		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4707		ChemSep v8.3 pure component data Compiled value
PAff	[820.10; 825.70]	kJ/mol
PAff	825.70	kJ/mol	NIST
PAff	820.10	kJ/mol	NIST
BasG	[793.70; 795.00]	kJ/mol
BasG	795.00	kJ/mol	NIST
BasG	793.70	kJ/mol	NIST
ΔcH°solid	[-7054.50; -7011.10]	kJ/mol
ΔcH°solid	-7048.10 ± 1.50	kJ/mol	NIST
ΔcH°solid	-7054.50 ± 1.30	kJ/mol	NIST
ΔcH°solid	-7051.30	kJ/mol	NIST
ΔcH°solid	-7049.50 ± 1.40	kJ/mol	NIST
ΔcH°solid	-7011.10 ± 2.60	kJ/mol	NIST
ΔcH°solid	-7050.90 ± 2.70	kJ/mol	NIST
ΔcH°solid	-7014.31	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
EA	[-0.01; 0.31]	eV
EA	-0.01 ± 0.04	eV	NIST
EA	0.27 ± 0.04	eV	NIST
EA	0.31 ± 0.01	eV	NIST
EA	0.20	eV	NIST
ΔfG°	302.19	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[163.60; 206.90]	kJ/mol
ΔfH°gas	201.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	202.20 ± 2.30	kJ/mol	NIST
ΔfH°gas	201.20 ± 4.70	kJ/mol	NIST
ΔfH°gas	206.90 ± 4.60	kJ/mol	NIST
ΔfH°gas	203.80	kJ/mol	NIST
ΔfH°gas	Outlier 163.60	kJ/mol	NIST
ΔfH°solid	[72.80; 116.10]	kJ/mol
ΔfH°solid	110.10 ± 2.20	kJ/mol	NIST
ΔfH°solid	109.80 ± 1.60	kJ/mol	NIST
ΔfH°solid	116.10 ± 1.40	kJ/mol	NIST
ΔfH°solid	113.00	kJ/mol	NIST
ΔfH°solid	72.80 ± 2.60	kJ/mol	NIST
ΔfusH°	15.15	kJ/mol	Thermodynamic study of (anthracene + phenanthrene) solid state mixtures
ΔsubH°	[87.40; 93.00]	kJ/mol
ΔsubH°	92.10 ± 0.60	kJ/mol	NIST
ΔsubH°	92.50 ± 0.40	kJ/mol	NIST
ΔsubH°	89.60 ± 0.80	kJ/mol	NIST
ΔsubH°	90.50	kJ/mol	NIST
ΔsubH°	91.40	kJ/mol	NIST
ΔsubH°	90.90 ± 1.70	kJ/mol	NIST
ΔsubH°	93.00 ± 2.00	kJ/mol	NIST
ΔsubH°	93.00 ± 2.00	kJ/mol	NIST
ΔsubH°	Outlier 87.40 ± 0.80	kJ/mol	NIST
ΔsubH°	90.88 ± 0.79	kJ/mol	NIST
ΔsubH°	90.90 ± 0.40	kJ/mol	NIST
ΔsubH°	90.80	kJ/mol	NIST
ΔvapH°	[78.50; 79.00]	kJ/mol
ΔvapH°	78.70	kJ/mol	NIST
ΔvapH°	79.00 ± 1.20	kJ/mol	NIST
ΔvapH°	78.70	kJ/mol	NIST
ΔvapH°	78.50	kJ/mol	NIST
IE	[7.60; 23.10]	eV
IE	7.89 ± 0.00	eV	NIST
IE	7.90	eV	NIST
IE	7.87 ± 0.02	eV	NIST
IE	7.89 ± 0.00	eV	NIST
IE	7.89 ± 0.05	eV	NIST
IE	7.86	eV	NIST
IE	7.92 ± 0.05	eV	NIST
IE	7.86 ± 0.01	eV	NIST
IE	7.92	eV	NIST
IE	7.91 ± 0.01	eV	NIST
IE	8.08	eV	NIST
IE	7.69	eV	NIST
IE	7.75	eV	NIST
IE	8.03 ± 0.01	eV	NIST
IE	8.10 ± 0.04	eV	NIST
IE	8.03 ± 0.01	eV	NIST
IE	8.07	eV	NIST
IE	7.60	eV	NIST
IE	8.22	eV	NIST
IE	8.25	eV	NIST
IE	8.09	eV	NIST
IE	8.03	eV	NIST
IE	Outlier 23.10	eV	NIST
IE	8.03	eV	NIST
IE	8.02	eV	NIST
IE	7.91	eV	NIST
IE	7.85	eV	NIST
IE	7.86 ± 0.02	eV	NIST
IE	7.86	eV	NIST
IE	7.87 ± 0.02	eV	NIST
IE	7.92 ± 0.02	eV	NIST
log10WS	[-5.26; -5.26]
log10WS	-5.26		Aq. Solubility Prediction
log10WS	-5.26		Estimated Solubility
logPoct/wat	3.993		Crippen Calculated Property
McVol	145.440	ml/mol	McGowan Calculated Property
Pc	[2900.00; 3171.47]	kPa
Pc	3171.47	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2900.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	0.03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[1724.00; 1797.00]
Inp	1730.00		NIST
Inp	1745.00		NIST
Inp	1765.00		NIST
Inp	1761.00		NIST
Inp	Outlier 1724.00		NIST
Inp	1778.60		NIST
Inp	1775.00		NIST
Inp	1759.60		NIST
Inp	1778.40		NIST
Inp	1790.10		NIST
Inp	1776.30		NIST
Inp	1776.30		NIST
Inp	1756.90		NIST
Inp	1776.30		NIST
Inp	1789.20		NIST
Inp	1769.70		NIST
Inp	1791.20		NIST
Inp	1797.00		NIST
Inp	1759.30		NIST
Inp	1756.90		NIST
Inp	1776.30		NIST
Inp	1789.20		NIST
Inp	1776.30		NIST
Inp	1776.30		NIST
Inp	1794.00		NIST
Inp	1791.00		NIST
Inp	1776.00		NIST
Inp	1742.00		NIST
Inp	1730.00		NIST
Inp	1739.00		NIST
Inp	1739.00		NIST
Inp	1739.00		NIST
Inp	1739.00		NIST
Inp	1740.00		NIST
Inp	1753.00		NIST
Inp	1753.00		NIST
Inp	1753.00		NIST
Inp	1753.00		NIST
Inp	1754.00		NIST
Inp	1756.00		NIST
Inp	1757.00		NIST
Inp	1761.00		NIST
Inp	1763.00		NIST
Inp	1768.00		NIST
Inp	1744.70		NIST
Inp	1734.95		NIST
Inp	1741.00		NIST
Inp	1744.37		NIST
Inp	1784.21		NIST
Inp	Outlier 1724.00		NIST
Inp	1761.00		NIST
Inp	1749.00		NIST
Inp	1729.00		NIST
Inp	1792.00		NIST
Inp	1775.00		NIST
Inp	1775.00		NIST
Inp	1749.00		NIST
Inp	1784.00		NIST
Inp	1784.00		NIST
Inp	1775.00		NIST
Inp	1784.00		NIST
Inp	1752.00		NIST
Inp	1760.00		NIST
Inp	1784.70		NIST
Inp	1776.00		NIST
Inp	1777.00		NIST
Inp	1779.00		NIST
Inp	1780.00		NIST
Inp	1781.00		NIST
Inp	1782.00		NIST
Inp	1792.00		NIST
Inp	1793.00		NIST
Inp	1769.00		NIST
Inp	1751.00		NIST
Inp	1744.00		NIST
Inp	1744.00		NIST
Inp	1767.00		NIST
Inp	1772.00		NIST
Inp	1741.00		NIST
Inp	1752.00		NIST
Inp	1784.00		NIST
Inp	1780.00		NIST
Inp	1768.00		NIST
Inp	1770.00		NIST
Inp	1755.00		NIST
Inp	1794.00		NIST
Inp	1797.00		NIST
Inp	1747.00		NIST
Inp	1786.00		NIST
Inp	1786.00		NIST
Inp	1741.00		NIST
Inp	1770.00		NIST
Inp	1786.00		NIST
Ip	[2712.00; 2723.00]
Ip	2722.00		NIST
Ip	2723.00		NIST
Ip	2712.00		NIST
Ip	2722.00		NIST
S°solid,1 bar	[211.70; 215.06]	J/mol×K
S°solid,1 bar	215.06	J/mol×K	NIST
S°solid,1 bar	211.70	J/mol×K	NIST
Tboil	[601.15; 613.20]	K
Tboil	610.03	K	ChemSep v8.3 pure component data Compiled value
Tboil	613.00	K	KDB
Tboil	609.20	K	NIST
Tboil	613.20	K	NIST
Tboil	605.15 ± 5.00	K	NIST
Tboil	601.15 ± 3.00	K	NIST
Tboil	613.15 ± 2.00	K	NIST
Tc	[0.87; 893.00]	K
Tc	893.00	K	Critical point measurement of some polycyclic aromatic hydrocarbons
Tc	Outlier 0.87	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Tc	873.10	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	869.00	K	ChemSep v8.3 pure component data Compiled value
Tc	869.00	K	KDB
Tc	869.00 ± 1.00	K	NIST
Tc	869.30 ± 1.00	K	NIST
Tfus	[369.40; 645.70]	K
Tfus	378.07	K	Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols + 2-Propanol and Ethanol + Methanol at 298.15 K
Tfus	372.39	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	372.38	K	ChemSep v8.3 pure component data Compiled value
Tfus	372.39	K	KDB
Tfus	372.71	K	Aq. Solubility Prediction
Tfus	Outlier 645.70 ± 0.40	K	NIST
Tfus	372.74 ± 0.20	K	NIST
Tfus	370.00 ± 1.50	K	NIST
Tfus	372.00 ± 1.50	K	NIST
Tfus	373.00 ± 2.00	K	NIST
Tfus	373.15 ± 1.00	K	NIST
Tfus	372.80 ± 0.30	K	NIST
Tfus	371.30 ± 1.00	K	NIST
Tfus	373.15 ± 0.30	K	NIST
Tfus	371.80 ± 2.00	K	NIST
Tfus	371.20 ± 1.50	K	NIST
Tfus	371.90 ± 0.70	K	NIST
Tfus	372.70 ± 1.00	K	NIST
Tfus	373.00 ± 2.50	K	NIST
Tfus	372.05 ± 1.00	K	NIST
Tfus	374.00 ± 1.50	K	NIST
Tfus	372.11 ± 0.50	K	NIST
Tfus	372.32 ± 0.20	K	NIST
Tfus	372.60 ± 0.30	K	NIST
Tfus	372.77 ± 0.20	K	NIST
Tfus	372.30 ± 0.10	K	NIST
Tfus	372.90 ± 0.50	K	NIST
Tfus	373.00 ± 1.50	K	NIST
Tfus	371.40 ± 0.20	K	NIST
Tfus	374.20 ± 1.00	K	NIST
Tfus	373.00 ± 0.50	K	NIST
Tfus	371.70 ± 0.10	K	NIST
Tfus	371.40 ± 1.50	K	NIST
Tfus	369.50 ± 1.00	K	NIST
Tfus	371.15 ± 0.50	K	NIST
Tfus	374.15 ± 3.00	K	NIST
Tfus	378.65 ± 2.00	K	NIST
Tfus	372.95 ± 0.30	K	NIST
Tfus	418.00 ± 8.36	K	NIST
Tfus	369.40 ± 0.50	K	NIST
Ttriple	[339.52; 372.38]	K
Ttriple	339.52	K	Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
Ttriple	372.38	K	ChemSep v8.3 pure component data Compiled value
Ttriple	372.38 ± 0.02	K	NIST
Ttriple	372.38 ± 0.02	K	NIST
Ttriple	372.38 ± 0.02	K	NIST
UQi	4.34		ChemSep v8.3 pure component data Compiled value
URi	6.56		ChemSep v8.3 pure component data Compiled value
Vc	[0.554; 0.554]	m3/kmol
Vc	0.554	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.554	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.554	m3/kmol	KDB
Zc	0.2220000		ChemSep v8.3 pure component data Compiled value
Zra	0.23		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[303.00; 347.00]	J/mol×K	[380.00; 490.00]
Cp,liquid	303.00	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	309.00	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	314.00	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	319.00	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	324.00	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	328.00	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	332.00	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	336.00	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	339.00	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	342.00	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	345.00	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	347.00	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,solid	[134.70; 267.40]	J/mol×K	[297.50; 343.00]
Cp,solid	233.50	J/mol×K	297.50	NIST
Cp,solid	207.10	J/mol×K	298.10	NIST
Cp,solid	226.40	J/mol×K	298.10	NIST
Cp,solid	220.30	J/mol×K	298.15	NIST
Cp,solid	220.62	J/mol×K	298.15	NIST
Cp,solid	134.70	J/mol×K	298.15	NIST
Cp,solid	267.40	J/mol×K	343.00	NIST
ΔfusH	[15.72; 18.63]	kJ/mol	[368.00; 373.81]
ΔfusH	16.60	kJ/mol	368.00	NIST
ΔfusH	17.15	kJ/mol	371.40	NIST
ΔfusH	17.14	kJ/mol	371.70	NIST
ΔfusH	16.46	kJ/mol	372.40	NIST
ΔfusH	16.20	kJ/mol	372.90	NIST
ΔfusH	18.63	kJ/mol	373.00	NIST
ΔfusH	18.00	kJ/mol	373.20	NIST
ΔfusH	15.72	kJ/mol	373.81	NIST
ΔsubH	[81.60; 96.20]	kJ/mol	[213.00; 383.00]
ΔsubH	95.80 ± 2.90	kJ/mol	213.00	NIST
ΔsubH	84.10	kJ/mol	293.00	NIST
ΔsubH	84.10 ± 2.50	kJ/mol	297.00	NIST
ΔsubH	90.90	kJ/mol	298.15	NIST
ΔsubH	95.90	kJ/mol	303.00	NIST
ΔsubH	95.00 ± 0.60	kJ/mol	303.00	NIST
ΔsubH	95.90	kJ/mol	303.00	NIST
ΔsubH	86.61	kJ/mol	309.70	NIST
ΔsubH	84.10 ± 0.80	kJ/mol	313.00	NIST
ΔsubH	90.70 ± 1.20	kJ/mol	315.00	NIST
ΔsubH	86.60	kJ/mol	316.50	NIST
ΔsubH	86.60	kJ/mol	316.50	NIST
ΔsubH	95.00 ± 4.40	kJ/mol	318.00	NIST
ΔsubH	81.60	kJ/mol	323.00	NIST
ΔsubH	84.10 ± 0.80	kJ/mol	323.00	NIST
ΔsubH	91.60 ± 0.40	kJ/mol	323.00	NIST
ΔsubH	96.20	kJ/mol	335.50	NIST
ΔsubH	82.00 ± 2.00	kJ/mol	339.50	NIST
ΔsubH	87.20	kJ/mol	344.50	NIST
ΔsubH	87.20 ± 1.10	kJ/mol	350.00	NIST
ΔsubH	87.20	kJ/mol	372.00	NIST
ΔsubH	88.90	kJ/mol	383.00	NIST
ΔvapH	[57.20; 92.30]	kJ/mol	[298.00; 559.50]
ΔvapH	78.65	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH	92.30	kJ/mol	298.15	Solution calorimetry as a complementary tool for the determination of enthalpies of vaporization and sublimation of low volatile compounds at 298.15 K
ΔvapH	87.24	kJ/mol	350.00	NIST
ΔvapH	71.20	kJ/mol	372.00	NIST
ΔvapH	71.20	kJ/mol	372.00	NIST
ΔvapH	71.20	kJ/mol	386.00	Evaluation of sublimation enthalpy by thermogravimetry: Analysis of the diffusion effects in the case of methyl and phenyl substituted hydantoins
ΔvapH	69.70	kJ/mol	390.00	NIST
ΔvapH	69.70	kJ/mol	390.00	NIST
ΔvapH	72.20	kJ/mol	398.00	NIST
ΔvapH	69.60	kJ/mol	398.00	NIST
ΔvapH	71.20	kJ/mol	398.00	NIST
ΔvapH	67.50	kJ/mol	420.00	NIST
ΔvapH	67.50	kJ/mol	420.00	NIST
ΔvapH	58.20	kJ/mol	502.00	NIST
ΔvapH	57.20	kJ/mol	548.00	NIST
ΔvapH	61.20	kJ/mol	548.00	NIST
ΔvapH	59.30	kJ/mol	559.50	NIST
ΔvapH	61.20	kJ/mol	559.50	NIST
Psub	[1.40e-05; 1.01e-03]	kPa	[295.73; 333.16]
Psub	1.40e-05	kPa	295.73	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.40e-05	kPa	295.73	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.40e-05	kPa	295.73	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.50e-05	kPa	295.73	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.50e-05	kPa	295.73	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.50e-05	kPa	295.73	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.40e-05	kPa	295.73	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.10e-05	kPa	302.13	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.10e-05	kPa	302.13	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.20e-05	kPa	302.13	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.20e-05	kPa	302.13	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.20e-05	kPa	302.13	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.20e-05	kPa	302.13	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.20e-05	kPa	302.13	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	6.20e-05	kPa	307.66	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	6.10e-05	kPa	307.66	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	6.10e-05	kPa	307.66	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	6.10e-05	kPa	307.66	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	6.40e-05	kPa	307.66	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	6.10e-05	kPa	307.66	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.19e-04	kPa	313.10	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.19e-04	kPa	313.10	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.18e-04	kPa	313.10	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.18e-04	kPa	313.10	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.19e-04	kPa	313.10	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.23e-04	kPa	313.46	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.24e-04	kPa	313.46	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.24e-04	kPa	313.46	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.55e-04	kPa	315.48	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.56e-04	kPa	315.48	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.51e-04	kPa	315.48	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.85e-04	kPa	317.41	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.91e-04	kPa	317.41	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.93e-04	kPa	317.41	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.08e-04	kPa	318.47	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	2.00e-04	kPa	318.47	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	2.03e-04	kPa	318.47	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	2.05e-04	kPa	318.47	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	2.08e-04	kPa	318.47	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	2.11e-04	kPa	318.47	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	2.12e-04	kPa	318.47	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	2.38e-04	kPa	319.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.39e-04	kPa	319.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.35e-04	kPa	319.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.92e-04	kPa	321.48	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.93e-04	kPa	321.48	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.96e-04	kPa	321.48	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.38e-04	kPa	323.00	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.40e-04	kPa	323.00	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.41e-04	kPa	323.00	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.46e-04	kPa	323.00	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.46e-04	kPa	323.00	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.43e-04	kPa	323.00	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.43e-04	kPa	323.00	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	3.52e-04	kPa	323.16	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.52e-04	kPa	323.16	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.43e-04	kPa	323.16	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	4.46e-04	kPa	325.46	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	4.53e-04	kPa	325.46	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	4.36e-04	kPa	325.46	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	5.43e-04	kPa	327.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	5.44e-04	kPa	327.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	5.50e-04	kPa	327.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	5.79e-04	kPa	328.20	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	5.94e-04	kPa	328.20	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	5.83e-04	kPa	328.20	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	5.99e-04	kPa	328.20	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	5.90e-04	kPa	328.20	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	5.74e-04	kPa	328.20	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	6.70e-04	kPa	329.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	6.75e-04	kPa	329.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	6.78e-04	kPa	329.47	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	8.34e-04	kPa	331.42	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	8.25e-04	kPa	331.42	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	8.14e-04	kPa	331.42	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	9.59e-04	kPa	332.95	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	9.64e-04	kPa	332.95	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	9.42e-04	kPa	332.95	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	9.60e-04	kPa	332.95	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	9.38e-04	kPa	332.95	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	9.58e-04	kPa	332.95	Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Psub	1.01e-03	kPa	333.16	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.00e-03	kPa	333.16	The design, construction, and testing of a new Knudsen effusion apparatus
Pvap	[0.06; 3.87]	kPa	[384.00; 480.00]
Pvap	0.06	kPa	384.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.08	kPa	388.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.10	kPa	392.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.11	kPa	396.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.15	kPa	400.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.14	kPa	400.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.16	kPa	400.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.15	kPa	400.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.15	kPa	400.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.18	kPa	404.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.18	kPa	405.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.18	kPa	405.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.19	kPa	405.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.18	kPa	405.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.21	kPa	408.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.22	kPa	410.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.23	kPa	410.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.22	kPa	410.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.22	kPa	410.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.24	kPa	412.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.28	kPa	415.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.28	kPa	415.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.27	kPa	415.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.28	kPa	415.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.29	kPa	416.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.34	kPa	420.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.35	kPa	420.00	Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
Pvap	0.34	kPa	420.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.35	kPa	420.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.34	kPa	420.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.43	kPa	425.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.42	kPa	425.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.43	kPa	425.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.43	kPa	425.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.52	kPa	430.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.53	kPa	430.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.54	kPa	430.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.53	kPa	430.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.67	kPa	435.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.66	kPa	435.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.65	kPa	435.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.64	kPa	435.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.80	kPa	440.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.81	kPa	440.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.80	kPa	440.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.82	kPa	440.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.98	kPa	445.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.00	kPa	445.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.01	kPa	445.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	0.99	kPa	445.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.20	kPa	450.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.22	kPa	450.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.24	kPa	450.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.24	kPa	450.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.52	kPa	455.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.50	kPa	455.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.52	kPa	455.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.47	kPa	455.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.79	kPa	460.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.84	kPa	460.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.85	kPa	460.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	1.82	kPa	460.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.21	kPa	465.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.24	kPa	465.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.23	kPa	465.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.17	kPa	465.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.70	kPa	470.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.66	kPa	470.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.62	kPa	470.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	2.70	kPa	470.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.20	kPa	475.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.25	kPa	475.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.15	kPa	475.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.25	kPa	475.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.82	kPa	480.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.77	kPa	480.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.87	kPa	480.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
Pvap	3.87	kPa	480.00	Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
ΔfusS	[46.10; 49.90]	J/mol×K	[371.40; 373.20]
ΔfusS	46.20	J/mol×K	371.40	NIST
ΔfusS	46.10	J/mol×K	371.70	NIST
ΔfusS	49.90	J/mol×K	373.00	NIST
ΔfusS	48.20	J/mol×K	373.20	NIST
ΔsubS	304.90	J/mol×K	298.15	NIST
ΔvapS	249.30	J/mol×K	350.00	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	485.70	K	1.60	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[118.92; 506.85]	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			6.62000e+01
Coefficient B			-5.09490e+02
Coefficient C			6.52724e+00
Coefficient D			-7.52740e-05
Coefficient E			6.03660e-09
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	118.92	J/mol×K	200.00	Calculated Property
Cp,gas	218.05	J/mol×K	344.44	Calculated Property
Cp,gas	298.90	J/mol×K	488.89	Calculated Property
Cp,gas	358.43	J/mol×K	633.33	Calculated Property
Cp,gas	402.26	J/mol×K	777.78	Calculated Property
Cp,gas	435.09	J/mol×K	922.22	Calculated Property
Cp,gas	460.13	J/mol×K	1066.67	Calculated Property
Cp,gas	479.53	J/mol×K	1211.11	Calculated Property
Cp,gas	494.77	J/mol×K	1355.56	Calculated Property
Cp,gas	506.85	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[299.88; 366.60]	J/mol×K	[372.38; 500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.15950e+02
Coefficient B			-4.38200e+01
Coefficient C			4.07124e+00
Coefficient D			4.27730e-03
Coefficient E			-2.39280e-06
Temperature range, min.			372.38
Temperature range, max.			500.00
Cp,liquid	299.88	J/mol×K	372.38	Calculated Property
Cp,liquid	307.24	J/mol×K	386.56	Calculated Property
Cp,liquid	314.63	J/mol×K	400.74	Calculated Property
Cp,liquid	322.06	J/mol×K	414.92	Calculated Property
Cp,liquid	329.51	J/mol×K	429.10	Calculated Property
Cp,liquid	336.97	J/mol×K	443.28	Calculated Property
Cp,liquid	344.42	J/mol×K	457.46	Calculated Property
Cp,liquid	351.85	J/mol×K	471.64	Calculated Property
Cp,liquid	359.25	J/mol×K	485.82	Calculated Property
Cp,liquid	366.60	J/mol×K	500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0019197; 0.0002090]	Pa×s	[372.38; 695.20]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-2.24390e+01
Coefficient B			2.56540e+03
Coefficient C			1.56990e+00
Coefficient D			3.86550e-09
Coefficient E			2.00000e+00
Temperature range, min.			372.38
Temperature range, max.			695.20
η	0.0019197	Pa×s	372.38	Calculated Property
η	0.0012109	Pa×s	408.25	Calculated Property
η	0.0008321	Pa×s	444.12	Calculated Property
η	0.0006105	Pa×s	479.99	Calculated Property
η	0.0004715	Pa×s	515.86	Calculated Property
η	0.0003793	Pa×s	551.72	Calculated Property
η	0.0003153	Pa×s	587.59	Calculated Property
η	0.0002692	Pa×s	623.46	Calculated Property
η	0.0002350	Pa×s	659.33	Calculated Property
η	0.0002090	Pa×s	695.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[70.50; 0.00]	kJ/mol	[372.38; 869.00]	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			9.24550e+01
Coefficient B			2.89790e-01
Coefficient C			1.13930e+00
Coefficient D			-1.99460e+00
Coefficient E			9.25370e-01
Critical temperature, Tc (K)			8.69000e+02
Temperature range, min.			372.38
Temperature range, max.			869.00
ΔvapH	70.50	kJ/mol	372.38	Calculated Property
ΔvapH	66.90	kJ/mol	427.56	Calculated Property
ΔvapH	63.37	kJ/mol	482.74	Calculated Property
ΔvapH	59.87	kJ/mol	537.92	Calculated Property
ΔvapH	56.29	kJ/mol	593.10	Calculated Property
ΔvapH	52.43	kJ/mol	648.28	Calculated Property
ΔvapH	47.96	kJ/mol	703.46	Calculated Property
ΔvapH	42.21	kJ/mol	758.64	Calculated Property
ΔvapH	33.57	kJ/mol	813.82	Calculated Property
ΔvapH	0.00	kJ/mol	869.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[451.00; 647.66]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49964e+01
Coefficient B			-5.57632e+03
Coefficient C			-7.18810e+01
Temperature range, min.			451.00
Temperature range, max.			647.66
Pvap	1.33	kPa	451.00	Calculated Property
Pvap	2.97	kPa	472.85	Calculated Property
Pvap	6.10	kPa	494.70	Calculated Property
Pvap	11.66	kPa	516.55	Calculated Property
Pvap	20.98	kPa	538.40	Calculated Property
Pvap	35.81	kPa	560.26	Calculated Property
Pvap	58.40	kPa	582.11	Calculated Property
Pvap	91.48	kPa	603.96	Calculated Property
Pvap	138.31	kPa	625.81	Calculated Property
Pvap	202.66	kPa	647.66	Calculated Property
Pvap	[0.03; 2900.00]	kPa	[372.38; 804.05]	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			2.68152e+02
Coefficient B			-2.09181e+04
Coefficient C			-3.68710e+01
Coefficient D			1.93212e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 869 K.
Temperature range, min.			372.38
Temperature range, max.			804.05
Pvap	0.03	kPa	372.38	Calculated Property
Pvap	0.39	kPa	420.34	Calculated Property
Pvap	2.71	kPa	468.31	Calculated Property
Pvap	11.76	kPa	516.27	Calculated Property
Pvap	37.88	kPa	564.23	Calculated Property
Pvap	101.59	kPa	612.20	Calculated Property
Pvap	245.05	kPa	660.16	Calculated Property
Pvap	560.98	kPa	708.13	Calculated Property
Pvap	1266.58	kPa	756.09	Calculated Property
Pvap	2900.00	kPa	804.05	Calculated Property
Pvap	[0.03; 2879.35]	kPa	[372.15; 869.25]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.07381e+02
Coefficient B			-1.29131e+04
Coefficient C			-1.29796e+01
Coefficient D			4.34300e-06
Coefficient E			0.00000e+00
Temperature range, min.			372.15
Temperature range, max.			869.25
Pvap	0.03	kPa	372.15	Calculated Property
Pvap	0.51	kPa	427.38	Calculated Property
Pvap	4.19	kPa	482.62	Calculated Property
Pvap	20.44	kPa	537.85	Calculated Property
Pvap	70.53	kPa	593.08	Calculated Property
Pvap	191.15	kPa	648.32	Calculated Property
Pvap	436.94	kPa	703.55	Calculated Property
Pvap	885.07	kPa	758.78	Calculated Property
Pvap	1645.28	kPa	814.02	Calculated Property
Pvap	2879.35	kPa	869.25	Calculated Property
Pvap	[0.03; 0.42]	kPa	[373.00; 423.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50111e+01
Coefficient B			-5.59171e+03
Coefficient C			-7.09600e+01
Reference			Osborn and Douslin, 1975, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			373.00
Temperature range, max.			423.00
Pvap	0.03	kPa	373.00	Calculated Property
Pvap	0.04	kPa	378.56	Calculated Property
Pvap	0.06	kPa	384.11	Calculated Property
Pvap	0.08	kPa	389.67	Calculated Property
Pvap	0.11	kPa	395.22	Calculated Property
Pvap	0.14	kPa	400.78	Calculated Property
Pvap	0.19	kPa	406.33	Calculated Property
Pvap	0.25	kPa	411.89	Calculated Property
Pvap	0.32	kPa	417.44	Calculated Property
Pvap	0.42	kPa	423.00	Calculated Property
Pvap	[3.63; 118.54]	kPa	[476.80; 619.90]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.54029e+01
Coefficient B			-6.15555e+03
Coefficient C			-4.07000e+01
Reference			Mortimer and Murphy, 1923
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			476.80
Temperature range, max.			619.90
Pvap	3.63	kPa	476.80	Calculated Property
Pvap	5.96	kPa	492.70	Calculated Property
Pvap	9.46	kPa	508.60	Calculated Property
Pvap	14.58	kPa	524.50	Calculated Property
Pvap	21.85	kPa	540.40	Calculated Property
Pvap	31.95	kPa	556.30	Calculated Property
Pvap	45.67	kPa	572.20	Calculated Property
Pvap	63.93	kPa	588.10	Calculated Property
Pvap	87.82	kPa	604.00	Calculated Property
Pvap	118.54	kPa	619.90	Calculated Property
Pvap	[0.03; 0.42]	kPa	[373.00; 423.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50111e+01
Coefficient B			-5.59171e+03
Coefficient C			-7.09600e+01
Reference			Osborn and Douslin, 1975
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			373.00
Temperature range, max.			423.00
Pvap	0.03	kPa	373.00	Calculated Property
Pvap	0.04	kPa	378.56	Calculated Property
Pvap	0.06	kPa	384.11	Calculated Property
Pvap	0.08	kPa	389.67	Calculated Property
Pvap	0.11	kPa	395.22	Calculated Property
Pvap	0.14	kPa	400.78	Calculated Property
Pvap	0.19	kPa	406.33	Calculated Property
Pvap	0.25	kPa	411.89	Calculated Property
Pvap	0.32	kPa	417.44	Calculated Property
Pvap	0.42	kPa	423.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1066.75; 321.90]	kg/m3	[372.38; 869.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			8.12369e+01
Coefficient B			2.52370e-01
Coefficient C			8.69000e+02
Coefficient D			2.48480e-01
Temperature range, min.			372.38
Temperature range, max.			869.00
ρl	1066.75	kg/m3	372.38	Calculated Property
ρl	1030.52	kg/m3	427.56	Calculated Property
ρl	992.12	kg/m3	482.74	Calculated Property
ρl	951.03	kg/m3	537.92	Calculated Property
ρl	906.47	kg/m3	593.10	Calculated Property
ρl	857.24	kg/m3	648.28	Calculated Property
ρl	801.23	kg/m3	703.46	Calculated Property
ρl	734.17	kg/m3	758.64	Calculated Property
ρl	644.38	kg/m3	813.82	Calculated Property
ρl	321.90	kg/m3	869.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 2.63e-05]	N/m	[372.38; 864.53]	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			-3.56740e-02
Coefficient B			5.51020e+00
Coefficient C			-2.28690e+00
Coefficient D			-6.65020e-04
Coefficient E			-6.38390e-07
Comment			Range stopped where the equation turns negative; ChemSep gives it to 869 K.
Temperature range, min.			372.38
Temperature range, max.			864.53
γ	0.04	N/m	372.38	Calculated Property
γ	0.03	N/m	427.06	Calculated Property
γ	0.03	N/m	481.75	Calculated Property
γ	0.02	N/m	536.43	Calculated Property
γ	0.02	N/m	591.11	Calculated Property
γ	0.02	N/m	645.80	Calculated Property
γ	0.01	N/m	700.48	Calculated Property
γ	0.01	N/m	755.16	Calculated Property
γ	0.00	N/m	809.85	Calculated Property
γ	2.63e-05	N/m	864.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.05]	W/m×K	[372.38; 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			9.28710e-05
Coefficient B			9.93170e-01
Coefficient C			6.71870e+02
Coefficient D			2.99720e+04
Temperature range, min.			372.38
Temperature range, max.			1000.00
λgas	0.01	W/m×K	372.38	Calculated Property
λgas	0.01	W/m×K	442.12	Calculated Property
λgas	0.02	W/m×K	511.85	Calculated Property
λgas	0.02	W/m×K	581.59	Calculated Property
λgas	0.03	W/m×K	651.32	Calculated Property
λgas	0.03	W/m×K	721.06	Calculated Property
λgas	0.04	W/m×K	790.79	Calculated Property
λgas	0.04	W/m×K	860.53	Calculated Property
λgas	0.05	W/m×K	930.26	Calculated Property
λgas	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.13; 0.12]	W/m×K	[372.38; 610.03]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			1.16830e-01
Coefficient B			-5.80680e+02
Coefficient C			-6.22220e-01
Coefficient D			-6.25600e-03
Coefficient E			4.16380e-07
Temperature range, min.			372.38
Temperature range, max.			610.03
λliquid	0.13	W/m×K	372.38	Calculated Property
λliquid	0.13	W/m×K	398.79	Calculated Property
λliquid	0.13	W/m×K	425.19	Calculated Property
λliquid	0.13	W/m×K	451.60	Calculated Property
λliquid	0.13	W/m×K	478.00	Calculated Property
λliquid	0.12	W/m×K	504.41	Calculated Property
λliquid	0.12	W/m×K	530.81	Calculated Property
λliquid	0.12	W/m×K	557.22	Calculated Property
λliquid	0.12	W/m×K	583.62	Calculated Property
λliquid	0.12	W/m×K	610.03	Calculated Property

Similar Compounds

Find more compounds similar to Phenanthrene.

Mixtures

• Phenanthrene + Carbon dioxide
• Phenanthrene + 2-Pyrrolidinone, 1-methyl-
• Phenanthrene + Formamide, N,N-dimethyl- + Carbazole
• Phenanthrene + Acetone + Carbazole
• Phenanthrene + Acetonitrile + Carbazole
• Phenanthrene + Toluene + Carbazole
• Phenanthrene + Formamide, N,N-dimethyl-
• Phenanthrene + Acetone
• Phenanthrene + Acetonitrile
• Phenanthrene + Toluene
• Phenanthrene + Carbazole
• Phenanthrene + Cyclohexane
• Phenanthrene + Heptane
• Phenanthrene + Anthracene
• Phenanthrene + Nitrogen
• Phenanthrene + helium
• Phenanthrene + Ethanol + Pentane, 2,2,4-trimethyl-
• Phenanthrene + Water
• Phenanthrene + Ethanol + Methyl Alcohol
• Phenanthrene + 2-Propanol + Methyl Alcohol

Find more mixtures with Phenanthrene.

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 3 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons. J. Chem. Eng. Data 1995, 40, 547-558.
• 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
• Solubility of iodopropynyl butylcarbamate in supercritical carbon dioxide
• Enthalpies of solution, partial molar volumes and isentropic compressibilities of polycyclic aromatic hydrocarbons in 1-methyl-2-pyrrolidone at 298.15K
• The design, construction, and testing of a new Knudsen effusion apparatus
• Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 K
• Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
• Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
• Critical point measurement of some polycyclic aromatic hydrocarbons
• Thermodynamic study of (anthracene + phenanthrene) solid state mixtures
• Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
• Combined experiments to measure low sublimation pressures and diffusion coefficients of organometallic compounds
• Solution calorimetry as a complementary tool for the determination of enthalpies of vaporization and sublimation of low volatile compounds at 298.15 K
• Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
• Evaluation of sublimation enthalpy by thermogravimetry: Analysis of the diffusion effects in the case of methyl and phenyl substituted hydantoins
• Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
• Phase Behavior Data of (CO2 + Toluene + Phenanthrene) and (CO2 + (Methanol + Phenanthrene) Systems at High Pressure
• Solubilities of Palmitic Acid + Capsaicin in Supercritical Carbon Dioxide
• Measurement of the Phase Behavior of the Ternary System Carbon Dioxide + Acetone + Phenanthrene
• Ionic Liquids/Water Distribution Ratios of Some Polycyclic Aromatic Hydrocarbons
• Solubility of Anthracene and Phenanthrene in Ethanol + 2,2,4-Trimethylpentane Mixtures at Different Temperatures
• Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols + 2-Propanol and Ethanol + Methanol at 298.15 K
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols at 298.2 K
• 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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