Chemical Properties of Fluorene (CAS 86-73-7)

InChI

InChI=1S/C13H10/c1-3-7-12-10(5-1)9-11-6-2-4-8-13(11)12/h1-8H,9H2

InChI Key

NIHNNTQXNPWCJQ-UHFFFAOYSA-N

Formula

C13H10

SMILES

c1ccc2c(c1)Cc1ccccc1-2

Molecular Weight¹

166.22

CAS

86-73-7

Other Names

• 2,2'-Methylenebiphenyl
• 2,3-Benzindene
• 9H-Fluorene
• Diphenylenemethane
• Methane, diphenylene-
• o-Biphenylenemethane
• o-Biphenylmethane

• 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).
• T_boil : Normal Boiling Point Temperature (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.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4042; 0.4196]
ω	0.4196		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4042		ChemSep v8.3 pure component data Compiled value
PAff	[828.00; 831.50]	kJ/mol
PAff	831.50	kJ/mol	NIST
PAff	828.00	kJ/mol	NIST
BasG	[800.80; 803.80]	kJ/mol
BasG	803.80	kJ/mol	NIST
BasG	800.80	kJ/mol	NIST
ΔcH°solid	[-6634.60; -6631.50]	kJ/mol
ΔcH°solid	-6634.60 ± 1.10	kJ/mol	NIST
ΔcH°solid	-6631.50 ± 4.00	kJ/mol	NIST
μ	0.25	debye	ChemSep v8.3 pure component data Compiled value
EA	0.28 ± 0.03	eV	NIST
ΔfG°	290.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[166.90; 186.90]	kJ/mol
ΔfH°gas	186.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	176.70 ± 3.10	kJ/mol	NIST
ΔfH°gas	175.00 ± 1.50	kJ/mol	NIST
ΔfH°gas	166.90 ± 4.10	kJ/mol	NIST
ΔfH°solid	[86.70; 90.20]	kJ/mol
ΔfH°solid	90.20 ± 2.80	kJ/mol	NIST
ΔfH°solid	89.90 ± 1.40	kJ/mol	NIST
ΔfH°solid	86.70 ± 4.10	kJ/mol	NIST
ΔfusH°	17.99	kJ/mol	Joback Calculated Property
ΔsubH°	[80.20; 87.60]	kJ/mol
ΔsubH°	86.50 ± 1.30	kJ/mol	NIST
ΔsubH°	86.10 ± 0.10	kJ/mol	NIST
ΔsubH°	87.60	kJ/mol	NIST
ΔsubH°	85.13	kJ/mol	NIST
ΔsubH°	85.10	kJ/mol	NIST
ΔsubH°	85.10 ± 0.40	kJ/mol	NIST
ΔsubH°	80.21 ± 0.16	kJ/mol	NIST
ΔsubH°	80.20	kJ/mol	NIST
ΔsubH°	80.20 ± 0.20	kJ/mol	NIST
ΔvapH°	[65.70; 74.40]	kJ/mol
ΔvapH°	72.40 ± 1.70	kJ/mol	NIST
ΔvapH°	74.40 ± 1.20	kJ/mol	NIST
ΔvapH°	72.30	kJ/mol	NIST
ΔvapH°	72.20	kJ/mol	NIST
ΔvapH°	65.70	kJ/mol	NIST
IE	[7.78; 8.52]	eV
IE	7.91 ± 0.02	eV	NIST
IE	7.88 ± 0.05	eV	NIST
IE	Outlier 8.52	eV	NIST
IE	7.89 ± 0.03	eV	NIST
IE	7.93 ± 0.01	eV	NIST
IE	8.42	eV	NIST
IE	7.78	eV	NIST
IE	7.91	eV	NIST
IE	7.93 ± 0.02	eV	NIST
log10WS	[-5.00; -4.92]
log10WS	-4.97		Aq. Solubility Prediction
log10WS	-5.00		Estimated Solubility
log10WS	-4.92		Rytting (2005)
logPoct/wat	3.258		Crippen Calculated Property
McVol	135.650	ml/mol	McGowan Calculated Property
Pc	[2989.09; 3000.00]	kPa
Pc	2989.09	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3000.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	0.28	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[262.00; 1617.00]
Inp	1597.00		NIST
Inp	1557.00		NIST
Inp	1557.00		NIST
Inp	1574.00		NIST
Inp	1595.00		NIST
Inp	1535.00		NIST
Inp	1585.00		NIST
Inp	1552.10		NIST
Inp	1561.00		NIST
Inp	1609.00		NIST
Inp	1580.00		NIST
Inp	1583.40		NIST
Inp	1579.50		NIST
Inp	1578.90		NIST
Inp	1565.20		NIST
Inp	1579.50		NIST
Inp	1587.90		NIST
Inp	1590.50		NIST
Inp	1611.00		NIST
Inp	1595.00		NIST
Inp	1565.20		NIST
Inp	1579.50		NIST
Inp	1587.90		NIST
Inp	1579.50		NIST
Inp	1578.90		NIST
Inp	1574.59		NIST
Inp	1577.83		NIST
Inp	1580.72		NIST
Inp	1593.30		NIST
Inp	1589.39		NIST
Inp	1595.90		NIST
Inp	1590.56		NIST
Inp	1594.00		NIST
Inp	1583.00		NIST
Inp	1587.00		NIST
Inp	1555.00		NIST
Inp	1555.87		NIST
Inp	1549.28		NIST
Inp	1555.00		NIST
Inp	1552.98		NIST
Inp	1586.39		NIST
Inp	1604.00		NIST
Inp	1568.00		NIST
Inp	1548.00		NIST
Inp	1563.00		NIST
Inp	1552.00		NIST
Inp	1542.00		NIST
Inp	1544.00		NIST
Inp	1617.00		NIST
Inp	1558.00		NIST
Inp	1580.00		NIST
Inp	1587.00		NIST
Inp	1598.00		NIST
Inp	1593.00		NIST
Inp	1593.00		NIST
Inp	1580.00		NIST
Inp	1581.00		NIST
Inp	1583.00		NIST
Inp	1583.00		NIST
Inp	1583.00		NIST
Inp	1584.00		NIST
Inp	1591.00		NIST
Inp	1592.00		NIST
Inp	1558.00		NIST
Inp	1559.00		NIST
Inp	1531.00		NIST
Inp	1572.00		NIST
Inp	1550.00		NIST
Inp	1562.00		NIST
Inp	1582.00		NIST
Inp	1584.00		NIST
Inp	1563.00		NIST
Inp	1559.00		NIST
Inp	1593.00		NIST
Inp	1594.00		NIST
Inp	1547.00		NIST
Inp	1580.00		NIST
Inp	270.24		NIST
Inp	270.10		NIST
Inp	270.80		NIST
Inp	271.00		NIST
Inp	268.17		NIST
Inp	269.60		NIST
Inp	270.32		NIST
Inp	269.94		NIST
Inp	269.94		NIST
Inp	270.57		NIST
Inp	270.28		NIST
Inp	270.23		NIST
Inp	270.16		NIST
Inp	270.24		NIST
Inp	270.26		NIST
Inp	270.30		NIST
Inp	270.58		NIST
Inp	270.66		NIST
Inp	270.68		NIST
Inp	270.73		NIST
Inp	270.01		NIST
Inp	270.32		NIST
Inp	268.20		NIST
Inp	268.20		NIST
Inp	270.49		NIST
Inp	269.55		NIST
Inp	267.40		NIST
Inp	269.92		NIST
Inp	268.37		NIST
Inp	270.18		NIST
Inp	270.30		NIST
Inp	270.40		NIST
Inp	269.90		NIST
Inp	270.00		NIST
Inp	268.23		NIST
Inp	267.45		NIST
Inp	269.94		NIST
Inp	268.17		NIST
Inp	270.77		NIST
Inp	267.04		NIST
Inp	266.20		NIST
Inp	269.73		NIST
Inp	268.17		NIST
Inp	270.60		NIST
Inp	270.39		NIST
Inp	269.94		NIST
Inp	270.39		NIST
Inp	270.30		NIST
Inp	269.83		NIST
Inp	262.00		NIST
Inp	262.11		NIST
Inp	268.20		NIST
Inp	269.40		NIST
Inp	269.60		NIST
Inp	269.60		NIST
Inp	262.04		NIST
Inp	262.11		NIST
Inp	267.70		NIST
Inp	268.18		NIST
Inp	268.17		NIST
Inp	269.73		NIST
Inp	269.22		NIST
Inp	270.10		NIST
Inp	269.70		NIST
Inp	270.00		NIST
Inp	269.70		NIST
Inp	267.53		NIST
Inp	268.17		NIST
Inp	270.80		NIST
Inp	268.17		NIST
Inp	267.19		NIST
Inp	267.39		NIST
Inp	268.17		NIST
Inp	1597.00		NIST
Inp	1535.00		NIST
Inp	1580.00		NIST
Inp	1550.00		NIST
Inp	1559.00		NIST
Inp	270.60		NIST
Inp	269.83		NIST
Inp	269.60		NIST
Inp	268.18		NIST
Inp	269.70		NIST
Inp	270.80		NIST
Inp	1587.00		NIST
Inp	1581.00		NIST
Inp	1591.00		NIST
Inp	1572.00		NIST
Inp	1583.40		NIST
Inp	1587.90		NIST
Inp	1579.50		NIST
Inp	1577.83		NIST
Inp	1590.56		NIST
Inp	1555.87		NIST
Ip	[264.34; 2374.00]
Ip	2374.00		NIST
Ip	2337.00		NIST
Ip	2337.00		NIST
Ip	2338.00		NIST
Ip	2328.00		NIST
Ip	2322.00		NIST
Ip	2322.00		NIST
Ip	2331.00		NIST
Ip	2311.00		NIST
Ip	Outlier 264.34		NIST
Ip	2322.00		NIST
Ip	2328.00		NIST
S°solid,1 bar	207.32	J/mol×K	NIST
Tboil	[386.35; 571.20]	K
Tboil	570.44	K	ChemSep v8.3 pure component data Compiled value
Tboil	386.35	K	KDB
Tboil	571.20	K	NIST
Tboil	567.20	K	NIST
Tboil	569.55 ± 0.50	K	NIST
Tc	[822.32; 836.00]	K
Tc	836.00	K	Critical point measurement of some polycyclic aromatic hydrocarbons
Tc	822.32	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	826.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[385.60; 390.20]	K
Tfus	387.53	K	Solid-liquid equilibrium of some polycyclic aromatic hydrocarbons in wash oil
Tfus	388.00	K	Fluorene: An extended experimental thermodynamic study
Tfus	389.15	K	Solubility of Fluorene in Different Solvents from 278.98 K to 338.35 K
Tfus	389.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	387.94	K	ChemSep v8.3 pure component data Compiled value
Tfus	388.19	K	Aq. Solubility Prediction
Tfus	387.90 ± 0.30	K	NIST
Tfus	389.00 ± 0.30	K	NIST
Tfus	Outlier 385.60 ± 0.30	K	NIST
Tfus	389.40 ± 3.00	K	NIST
Tfus	390.20 ± 1.50	K	NIST
Tfus	388.15 ± 1.00	K	NIST
Tfus	390.00 ± 1.50	K	NIST
Tfus	388.10 ± 0.30	K	NIST
Tfus	388.00 ± 2.00	K	NIST
Tfus	387.00 ± 0.20	K	NIST
Tfus	387.00 ± 2.00	K	NIST
Tfus	387.00 ± 2.00	K	NIST
Tfus	387.35 ± 0.50	K	NIST
Ttriple	[355.51; 387.94]	K
Ttriple	387.94	K	ChemSep v8.3 pure component data Compiled value
Ttriple	Outlier 355.51 ± 0.03	K	NIST
Ttriple	387.94 ± 0.02	K	NIST
Ttriple	387.94 ± 0.02	K	NIST
Ttriple	387.94 ± 0.02	K	NIST
UQi	4.08		ChemSep v8.3 pure component data Compiled value
URi	6.17		ChemSep v8.3 pure component data Compiled value
Vc	[0.524; 0.550]	m3/kmol
Vc	0.550	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.524	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2290000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[295.20; 337.90]	J/mol×K	[390.00; 470.00]
Cp,liquid	295.20	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	299.90	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	304.70	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	309.80	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	315.00	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	320.50	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	326.10	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	331.90	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	337.90	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,solid	[171.44; 261.32]	J/mol×K	[262.36; 358.50]
Cp,solid	171.44	J/mol×K	262.36	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	171.61	J/mol×K	262.44	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	171.61	J/mol×K	262.47	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	173.52	J/mol×K	265.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	173.36	J/mol×K	265.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	173.36	J/mol×K	265.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	176.77	J/mol×K	270.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	176.68	J/mol×K	270.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	176.68	J/mol×K	270.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	180.09	J/mol×K	275.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	180.01	J/mol×K	275.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	179.93	J/mol×K	275.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	183.33	J/mol×K	280.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	183.25	J/mol×K	280.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	183.25	J/mol×K	280.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	186.49	J/mol×K	285.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	186.41	J/mol×K	285.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	186.33	J/mol×K	285.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	189.65	J/mol×K	290.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	189.49	J/mol×K	290.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	189.40	J/mol×K	290.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	192.90	J/mol×K	295.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	192.81	J/mol×K	295.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	192.73	J/mol×K	295.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	189.50	J/mol×K	298.10	NIST
Cp,solid	203.13	J/mol×K	298.15	NIST
Cp,solid	196.47	J/mol×K	300.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	196.47	J/mol×K	300.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	196.31	J/mol×K	300.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	201.38	J/mol×K	305.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	201.38	J/mol×K	305.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	201.21	J/mol×K	305.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	208.11	J/mol×K	310.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	208.20	J/mol×K	310.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	207.95	J/mol×K	310.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	216.18	J/mol×K	315.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	216.34	J/mol×K	315.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	216.09	J/mol×K	315.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	223.33	J/mol×K	320.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	223.66	J/mol×K	320.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	223.41	J/mol×K	320.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	227.90	J/mol×K	325.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	228.32	J/mol×K	325.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	228.32	J/mol×K	325.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	231.81	J/mol×K	330.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	232.39	J/mol×K	330.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	232.31	J/mol×K	330.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	236.96	J/mol×K	335.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	237.30	J/mol×K	335.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	237.21	J/mol×K	335.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	242.04	J/mol×K	340.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	241.87	J/mol×K	340.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	241.87	J/mol×K	340.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	246.77	J/mol×K	345.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	246.61	J/mol×K	345.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	246.61	J/mol×K	345.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	251.85	J/mol×K	350.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	251.76	J/mol×K	350.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	251.68	J/mol×K	350.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	257.25	J/mol×K	355.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	257.17	J/mol×K	355.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	257.08	J/mol×K	355.00	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	261.08	J/mol×K	358.37	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	261.32	J/mol×K	358.50	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
Cp,solid	261.24	J/mol×K	358.50	Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
ΔfusH	[19.10; 19.87]	kJ/mol	[387.00; 387.90]
ΔfusH	19.87	kJ/mol	387.00	NIST
ΔfusH	19.10	kJ/mol	387.70	NIST
ΔfusH	19.58	kJ/mol	387.90	NIST
ΔfusH	19.58	kJ/mol	387.90	NIST
ΔsubH	[78.90; 92.20]	kJ/mol	[293.00; 388.00]
ΔsubH	80.30 ± 0.80	kJ/mol	293.00	NIST
ΔsubH	88.40 ± 0.60	kJ/mol	303.00	NIST
ΔsubH	82.84	kJ/mol	306.30	NIST
ΔsubH	82.80	kJ/mol	314.00	NIST
ΔsubH	82.80	kJ/mol	314.50	NIST
ΔsubH	92.20	kJ/mol	320.50	NIST
ΔsubH	87.00 ± 1.00	kJ/mol	325.50	NIST
ΔsubH	83.20	kJ/mol	327.50	NIST
ΔsubH	84.90 ± 0.40	kJ/mol	343.00	NIST
ΔsubH	78.90	kJ/mol	368.00	NIST
ΔsubH	83.10 ± 1.30	kJ/mol	369.00	NIST
ΔsubH	83.10 ± 1.30	kJ/mol	369.00	NIST
ΔsubH	84.90	kJ/mol	383.00	NIST
ΔsubH	81.80	kJ/mol	388.00	NIST
ΔvapH	[54.20; 66.90]	kJ/mol	[398.00; 498.00]
ΔvapH	66.90	kJ/mol	398.00	NIST
ΔvapH	63.30	kJ/mol	405.00	NIST
ΔvapH	54.20	kJ/mol	485.00	NIST
ΔvapH	56.60	kJ/mol	498.00	NIST
Psub	[6.52e-05; 1.27e-03]	kPa	[298.00; 324.40]
Psub	6.61e-05	kPa	298.00	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	6.52e-05	kPa	298.10	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	8.40e-05	kPa	299.80	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	9.88e-05	kPa	301.40	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	1.41e-04	kPa	304.30	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	1.78e-04	kPa	306.60	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	1.95e-04	kPa	306.90	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	2.18e-04	kPa	308.10	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	2.61e-04	kPa	309.80	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	3.01e-04	kPa	311.20	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	4.14e-04	kPa	314.30	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	4.60e-04	kPa	316.00	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	5.31e-04	kPa	316.50	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	5.81e-04	kPa	317.30	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	6.13e-04	kPa	317.60	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	7.60e-04	kPa	320.30	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	1.27e-03	kPa	324.40	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Pvap	[4.63e-04; 20.71]	kPa	[298.15; 510.00]
Pvap	4.63e-04	kPa	298.15	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	5.52e-04	kPa	300.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	1.37e-03	kPa	310.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	3.21e-03	kPa	320.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	7.07e-03	kPa	330.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.01	kPa	340.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.03	kPa	350.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.06	kPa	360.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.10	kPa	370.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.18	kPa	380.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.30	kPa	390.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.48	kPa	400.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.76	kPa	410.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	1.17	kPa	420.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	1.75	kPa	430.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	2.55	kPa	440.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	3.64	kPa	450.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	5.08	kPa	460.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	6.96	kPa	470.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	9.37	kPa	480.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	12.39	kPa	490.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	16.14	kPa	500.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	20.71	kPa	510.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
ΔfusS	51.30	J/mol×K	387.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[103.15; 484.82]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			5.78250e+01
Coefficient B			-5.60420e+02
Coefficient C			6.66724e+00
Coefficient D			-2.71610e-04
Coefficient E			7.58040e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	103.15	J/mol×K	200.00	Calculated Property
Cp,gas	199.80	J/mol×K	344.44	Calculated Property
Cp,gas	280.62	J/mol×K	488.89	Calculated Property
Cp,gas	339.50	J/mol×K	633.33	Calculated Property
Cp,gas	382.01	J/mol×K	777.78	Calculated Property
Cp,gas	413.33	J/mol×K	922.22	Calculated Property
Cp,gas	437.15	J/mol×K	1066.67	Calculated Property
Cp,gas	455.94	J/mol×K	1211.11	Calculated Property
Cp,gas	471.44	J/mol×K	1355.56	Calculated Property
Cp,gas	484.82	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[294.24; 324.03]	J/mol×K	[387.94; 450.00]	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			1.72320e+02
Coefficient B			8.13110e+02
Coefficient C			-3.61086e+00
Coefficient D			2.32750e-02
Coefficient E			-1.80140e-05
Temperature range, min.			387.94
Temperature range, max.			450.00
Cp,liquid	294.24	J/mol×K	387.94	Calculated Property
Cp,liquid	297.53	J/mol×K	394.84	Calculated Property
Cp,liquid	300.86	J/mol×K	401.73	Calculated Property
Cp,liquid	304.20	J/mol×K	408.63	Calculated Property
Cp,liquid	307.55	J/mol×K	415.52	Calculated Property
Cp,liquid	310.90	J/mol×K	422.42	Calculated Property
Cp,liquid	314.24	J/mol×K	429.31	Calculated Property
Cp,liquid	317.54	J/mol×K	436.21	Calculated Property
Cp,liquid	320.81	J/mol×K	443.10	Calculated Property
Cp,liquid	324.03	J/mol×K	450.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0011637; 0.0002768]	Pa×s	[387.94; 570.44]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-3.30530e+01
Coefficient B			2.45490e+03
Coefficient C			3.45750e+00
Coefficient D			-4.25810e-06
Coefficient E			2.00000e+00
Temperature range, min.			387.94
Temperature range, max.			570.44
η	0.0011637	Pa×s	387.94	Calculated Property
η	0.0009462	Pa×s	408.22	Calculated Property
η	0.0007831	Pa×s	428.50	Calculated Property
η	0.0006575	Pa×s	448.77	Calculated Property
η	0.0005587	Pa×s	469.05	Calculated Property
η	0.0004793	Pa×s	489.33	Calculated Property
η	0.0004144	Pa×s	509.61	Calculated Property
η	0.0003605	Pa×s	529.88	Calculated Property
η	0.0003153	Pa×s	550.16	Calculated Property
η	0.0002768	Pa×s	570.44	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[61.94; 0.00]	kJ/mol	[387.94; 826.00]	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			9.58100e+01
Coefficient B			1.31700e+00
Coefficient C			-1.47390e+00
Coefficient D			-3.49690e-03
Coefficient E			6.15860e-01
Critical temperature, Tc (K)			8.26000e+02
Temperature range, min.			387.94
Temperature range, max.			826.00
ΔvapH	61.94	kJ/mol	387.94	Calculated Property
ΔvapH	59.75	kJ/mol	436.61	Calculated Property
ΔvapH	57.59	kJ/mol	485.29	Calculated Property
ΔvapH	55.27	kJ/mol	533.96	Calculated Property
ΔvapH	52.53	kJ/mol	582.63	Calculated Property
ΔvapH	49.04	kJ/mol	631.31	Calculated Property
ΔvapH	44.32	kJ/mol	679.98	Calculated Property
ΔvapH	37.65	kJ/mol	728.65	Calculated Property
ΔvapH	27.55	kJ/mol	777.33	Calculated Property
ΔvapH	0.00	kJ/mol	826.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[417.55; 608.78]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.48211e+01
Coefficient B			-5.26077e+03
Coefficient C			-5.55750e+01
Temperature range, min.			417.55
Temperature range, max.			608.78
Pvap	1.33	kPa	417.55	Calculated Property
Pvap	2.98	kPa	438.80	Calculated Property
Pvap	6.14	kPa	460.05	Calculated Property
Pvap	11.75	kPa	481.29	Calculated Property
Pvap	21.14	kPa	502.54	Calculated Property
Pvap	36.06	kPa	523.79	Calculated Property
Pvap	58.73	kPa	545.04	Calculated Property
Pvap	91.85	kPa	566.28	Calculated Property
Pvap	138.60	kPa	587.53	Calculated Property
Pvap	202.64	kPa	608.78	Calculated Property
Pvap	[0.26; 3000.00]	kPa	[387.94; 820.19]	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			1.34967e+02
Coefficient B			-1.38338e+04
Coefficient C			-1.70480e+01
Coefficient D			6.37820e-06
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 870 K.
Temperature range, min.			387.94
Temperature range, max.			820.19
Pvap	0.26	kPa	387.94	Calculated Property
Pvap	2.31	kPa	435.97	Calculated Property
Pvap	12.01	kPa	483.99	Calculated Property
Pvap	43.14	kPa	532.02	Calculated Property
Pvap	119.67	kPa	580.05	Calculated Property
Pvap	276.55	kPa	628.08	Calculated Property
Pvap	561.33	kPa	676.10	Calculated Property
Pvap	1039.37	kPa	724.13	Calculated Property
Pvap	1804.78	kPa	772.16	Calculated Property
Pvap	3000.00	kPa	820.19	Calculated Property
Pvap	[0.27; 4629.37]	kPa	[387.15; 870.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			7.33490e+01
Coefficient B			-1.04673e+04
Coefficient C			-8.04407e+00
Coefficient D			2.07264e-06
Coefficient E			0.00000e+00
Temperature range, min.			387.15
Temperature range, max.			870.00
Pvap	0.27	kPa	387.15	Calculated Property
Pvap	2.80	kPa	440.80	Calculated Property
Pvap	16.20	kPa	494.45	Calculated Property
Pvap	63.09	kPa	548.10	Calculated Property
Pvap	185.67	kPa	601.75	Calculated Property
Pvap	446.16	kPa	655.40	Calculated Property
Pvap	923.27	kPa	709.05	Calculated Property
Pvap	1708.33	kPa	762.70	Calculated Property
Pvap	2904.36	kPa	816.35	Calculated Property
Pvap	4629.37	kPa	870.00	Calculated Property
Pvap	[2.37; 108.81]	kPa	[434.00; 573.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.66961e+01
Coefficient B			-6.93326e+03
Coefficient C			3.85700e+00
Reference			Mortimer and Murphy, 1923
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			434.00
Temperature range, max.			573.60
Pvap	2.37	kPa	434.00	Calculated Property
Pvap	4.07	kPa	449.51	Calculated Property
Pvap	6.75	kPa	465.02	Calculated Property
Pvap	10.83	kPa	480.53	Calculated Property
Pvap	16.89	kPa	496.04	Calculated Property
Pvap	25.64	kPa	511.56	Calculated Property
Pvap	37.99	kPa	527.07	Calculated Property
Pvap	55.03	kPa	542.58	Calculated Property
Pvap	78.11	kPa	558.09	Calculated Property
Pvap	108.81	kPa	573.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1084.48; 317.07]	kg/m3	[387.94; 826.00]	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			7.26092e+01
Coefficient B			2.29000e-01
Coefficient C			8.26000e+02
Coefficient D			2.85710e-01
Temperature range, min.			387.94
Temperature range, max.			826.00
ρl	1084.48	kg/m3	387.94	Calculated Property
ρl	1041.23	kg/m3	436.61	Calculated Property
ρl	995.90	kg/m3	485.29	Calculated Property
ρl	947.98	kg/m3	533.96	Calculated Property
ρl	896.72	kg/m3	582.63	Calculated Property
ρl	840.95	kg/m3	631.31	Calculated Property
ρl	778.66	kg/m3	679.98	Calculated Property
ρl	705.77	kg/m3	728.65	Calculated Property
ρl	611.27	kg/m3	777.33	Calculated Property
ρl	317.07	kg/m3	826.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 2.03e-05]	N/m	[387.94; 821.18]	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			-6.77530e-03
Coefficient B			5.69690e+02
Coefficient C			-6.19810e+00
Coefficient D			7.81400e-03
Coefficient E			-8.75500e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 826 K.
Temperature range, min.			387.94
Temperature range, max.			821.18
γ	0.04	N/m	387.94	Calculated Property
γ	0.04	N/m	436.08	Calculated Property
γ	0.03	N/m	484.22	Calculated Property
γ	0.02	N/m	532.35	Calculated Property
γ	0.02	N/m	580.49	Calculated Property
γ	0.01	N/m	628.63	Calculated Property
γ	0.01	N/m	676.77	Calculated Property
γ	0.01	N/m	724.91	Calculated Property
γ	0.00	N/m	773.04	Calculated Property
γ	2.03e-05	N/m	821.18	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.06]	W/m×K	[387.94; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.74370e-04
Coefficient B			9.15200e-01
Coefficient C			5.00250e+02
Coefficient D			6.26130e+04
Temperature range, min.			387.94
Temperature range, max.			1000.00
λgas	0.02	W/m×K	387.94	Calculated Property
λgas	0.02	W/m×K	455.95	Calculated Property
λgas	0.02	W/m×K	523.95	Calculated Property
λgas	0.03	W/m×K	591.96	Calculated Property
λgas	0.03	W/m×K	659.97	Calculated Property
λgas	0.04	W/m×K	727.97	Calculated Property
λgas	0.05	W/m×K	795.98	Calculated Property
λgas	0.05	W/m×K	863.99	Calculated Property
λgas	0.06	W/m×K	931.99	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.11]	W/m×K	[387.94; 570.44]	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			-1.32580e-02
Coefficient B			-1.30680e+02
Coefficient C			-6.84760e-01
Coefficient D			-2.25660e-03
Coefficient E			3.00430e-07
Temperature range, min.			387.94
Temperature range, max.			570.44
λliquid	0.14	W/m×K	387.94	Calculated Property
λliquid	0.14	W/m×K	408.22	Calculated Property
λliquid	0.14	W/m×K	428.50	Calculated Property
λliquid	0.13	W/m×K	448.77	Calculated Property
λliquid	0.13	W/m×K	469.05	Calculated Property
λliquid	0.12	W/m×K	489.33	Calculated Property
λliquid	0.12	W/m×K	509.61	Calculated Property
λliquid	0.12	W/m×K	529.88	Calculated Property
λliquid	0.11	W/m×K	550.16	Calculated Property
λliquid	0.11	W/m×K	570.44	Calculated Property

Similar Compounds

Find more compounds similar to Fluorene.

Mixtures

• Anthracene + Fluorene
• Fluorene + Carbazole
• 9H-Fluoren-9-one + Fluorene
• Ethanol + Fluorene
• Ethanol + 9H-Fluoren-9-one + Fluorene
• Fluorene + Water
• Toluene + Fluorene
• 2-Propanol + Fluorene
• 1-Butanol + Fluorene
• Benzene + Fluorene
• Trichloromethane + Fluorene
• Fluorene + Acetone
• 1-Propanol + Fluorene
• Fluorene + 1-Propanol, 2-methyl-

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).
• 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
• Solid-liquid phase equilibrium of 9-fluorenone and several polynuclear aromatic hydrocarbons
• Solid-liquid equilibrium of some polycyclic aromatic hydrocarbons in wash oil
• Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene
• Fluorene: An extended experimental thermodynamic study
• Critical point measurement of some polycyclic aromatic hydrocarbons
• Modified solution calorimetry approach for determination of vaporization and sublimation enthalpies of branched-chain aliphatic and alkyl aromatic compounds at T = 298.15 K
• Determination of sublimation enthalpies of substituted benzophenones, fluorenes and diphenyl ethers by solution calorimetry approach
• Ionic Liquids/Water Distribution Ratios of Some Polycyclic Aromatic Hydrocarbons
• Solid Liquid Phase Equilibrium and Solubility of Dibenzo[b,d]furan and 9H-Fluoren-9-one in Organic Solvents
• Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
• Solubility of Fluorene in Different Solvents from 278.98 K to 338.35 K
• Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
• Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
• Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• Aqueous and cosolvent solubility data for drug-like organic compounds
• 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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