Fluoranthene (CAS 206-44-0)

InChI

InChI=1S/C16H10/c1-2-8-13-12(7-1)14-9-3-5-11-6-4-10-15(13)16(11)14/h1-10H

InChI Key

GVEPBJHOBDJJJI-UHFFFAOYSA-N

Formula

C16H10

SMILES

c1ccc2c(c1)-c1cccc3cccc-2c13

Molecular Weight¹

202.25

CAS

206-44-0

Other Names

1,2-(1,8-NAPHTHYLENE)-BENZENE
1,2-(1,8-Naphthalene)benzene
1,2-(1,8-Naphthalenediyl)benzene
1,2-(1,8-naphthylene)benzene
1,2-benzacenaphthene
Benzene, 1,2-(1,8-naphthalenediyl)-
Benzene, 1,2-(1,8-naphthylene)-
Fluoranthrene
Idryl
NSC 6803
Rcra waste number U120
benzo[jk]fluorene

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).
C_sat : Molar heat capacity at saturation pressure (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.
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.
Z_ra : Rackett Parameter.
¹: Molecular weight from the IUPAC atomic weights tables.

Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Please note that you need to enable javascript to get access to all the properties. Here is how to do it for Internet Explorer and for Firefox.

Physical Properties

Property	Value	Unit	Source
ω	[0.5160; 0.5875]
ω	0.5160		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5875		ChemSep v8.3 pure component data Compiled value
PAff	[826.80; 828.60]	kJ/mol
PAff	828.60	kJ/mol	NIST
PAff	826.80	kJ/mol	NIST
BasG	[799.60; 800.90]	kJ/mol
BasG	800.90	kJ/mol	NIST
BasG	799.60	kJ/mol	NIST
Δ_cH°_solid	[-7917.80; -7915.20]	kJ/mol
Δ_cH°_solid	-7915.20 ± 0.40	kJ/mol	NIST
Δ_cH°_solid	-7917.80 ± 5.40	kJ/mol	NIST
μ	0.23	debye	ChemSep v8.3 pure component data Compiled value
EA	0.63	eV	NIST
Δ_fG°	386.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_gas	[288.90; 292.00]	kJ/mol
Δ_fH°_gas	288.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_gas	291.40 ± 4.00	kJ/mol	NIST
Δ_fH°_gas	289.80	kJ/mol	NIST
Δ_fH°_gas	292.00 ± 2.20	kJ/mol	NIST
Δ_fH°_solid	[189.80; 192.00]	kJ/mol
Δ_fH°_solid	190.20 ± 2.80	kJ/mol	NIST
Δ_fH°_solid	189.80 ± 0.40	kJ/mol	NIST
Δ_fH°_solid	192.00 ± 5.40	kJ/mol	NIST
Δ_fusH°	24.49	kJ/mol	Joback Calculated Property
Δ_subH°	[99.20; 102.00]	kJ/mol
Δ_subH°	101.20 ± 2.80	kJ/mol	NIST
Δ_subH°	99.20 ± 0.80	kJ/mol	NIST
Δ_subH°	99.20 ± 0.80	kJ/mol	NIST
Δ_subH°	102.00 ± 2.00	kJ/mol	NIST
Δ_subH°	100.00	kJ/mol	NIST
Δ_vapH°	86.80 ± 1.30	kJ/mol	NIST
IE	[7.72; 7.95]	eV
IE	7.90 ± 0.10	eV	NIST
IE	7.90 ± 0.10	eV	NIST
IE	7.95 ± 0.04	eV	NIST
IE	7.80 ± 0.01	eV	NIST
IE	7.72	eV	NIST
log₁₀WS	[-6.00; -5.95]
log₁₀WS	-5.95		Aq. Solubility Prediction
log₁₀WS	-6.00		Estimated Solubility
logP_oct/wat	4.487		Crippen Calculated Property
McVol	158.460	ml/mol	McGowan Calculated Property
P_c	[2573.66; 2610.00]	kPa
P_c	2573.66	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
P_c	2610.00	kPa	ChemSep v8.3 pure component data Compiled value
P_triple	0.02	kPa	ChemSep v8.3 pure component data Compiled value
I_np	[337.00; 2098.00]
I_np	2057.00		NIST
I_np	2091.00		NIST
I_np	2091.00		NIST
I_np	2051.00		NIST
I_np	2091.00		NIST
I_np	2053.50		NIST
I_np	2060.10		NIST
I_np	2060.10		NIST
I_np	2032.60		NIST
I_np	2060.10		NIST
I_np	2076.50		NIST
I_np	2038.90		NIST
I_np	2062.30		NIST
I_np	2085.00		NIST
I_np	2032.60		NIST
I_np	2060.10		NIST
I_np	2076.50		NIST
I_np	2060.10		NIST
I_np	2060.10		NIST
I_np	2084.00		NIST
I_np	2011.00		NIST
I_np	2009.00		NIST
I_np	2009.00		NIST
I_np	2009.00		NIST
I_np	2009.00		NIST
I_np	2009.00		NIST
I_np	2023.00		NIST
I_np	2023.00		NIST
I_np	2023.00		NIST
I_np	2023.00		NIST
I_np	2030.00		NIST
I_np	2030.00		NIST
I_np	2031.00		NIST
I_np	2037.00		NIST
I_np	2042.00		NIST
I_np	2044.00		NIST
I_np	2020.00		NIST
I_np	2020.45		NIST
I_np	2068.42		NIST
I_np	2084.00		NIST
I_np	2037.00		NIST
I_np	2015.00		NIST
I_np	2098.00		NIST
I_np	2089.00		NIST
I_np	2052.00		NIST
I_np	2053.00		NIST
I_np	2057.00		NIST
I_np	2058.00		NIST
I_np	2060.00		NIST
I_np	2061.00		NIST
I_np	2079.00		NIST
I_np	2080.00		NIST
I_np	2031.00		NIST
I_np	2045.00		NIST
I_np	2062.00		NIST
I_np	2028.00		NIST
I_np	2006.00		NIST
I_np	2084.00		NIST
I_np	2085.00		NIST
I_np	2030.00		NIST
I_np	2091.00		NIST
I_np	341.94		NIST
I_np	340.99		NIST
I_np	343.44		NIST
I_np	343.15		NIST
I_np	342.27		NIST
I_np	343.16		NIST
I_np	344.01		NIST
I_np	344.30		NIST
I_np	337.00		NIST
I_np	337.00		NIST
I_np	344.01		NIST
I_np	340.90		NIST
I_np	344.85		NIST
I_np	344.49		NIST
I_np	344.78		NIST
I_np	344.83		NIST
I_np	344.99		NIST
I_np	344.49		NIST
I_np	344.51		NIST
I_np	344.56		NIST
I_np	344.60		NIST
I_np	344.64		NIST
I_np	344.67		NIST
I_np	344.74		NIST
I_np	344.75		NIST
I_np	344.54		NIST
I_np	344.68		NIST
I_np	344.80		NIST
I_np	344.80		NIST
I_np	344.67		NIST
I_np	344.85		NIST
I_np	344.80		NIST
I_np	345.00		NIST
I_np	344.55		NIST
I_np	344.62		NIST
I_np	344.35		NIST
I_np	344.49		NIST
I_np	344.68		NIST
I_np	344.43		NIST
I_np	340.66		NIST
I_np	344.56		NIST
I_np	344.70		NIST
I_np	344.51		NIST
I_np	344.01		NIST
I_np	344.60		NIST
I_np	344.96		NIST
I_np	344.49		NIST
I_np	344.96		NIST
I_np	340.10		NIST
I_np	338.20		NIST
I_np	389.98		NIST
I_np	340.21		NIST
I_np	340.44		NIST
I_np	338.50		NIST
I_np	344.00		NIST
I_np	344.90		NIST
I_np	340.35		NIST
I_np	340.44		NIST
I_np	342.65		NIST
I_np	343.25		NIST
I_np	343.31		NIST
I_np	344.01		NIST
I_np	344.51		NIST
I_np	343.24		NIST
I_np	344.60		NIST
I_np	340.11		NIST
I_np	344.01		NIST
I_np	345.32		NIST
I_np	344.60		NIST
I_np	340.05		NIST
I_np	340.88		NIST
I_np	341.74		NIST
I_np	342.74		NIST
I_np	343.25		NIST
I_np	343.65		NIST
I_np	344.01		NIST
I_np	345.00		NIST
I_np	2062.00		NIST
I_np	2030.00		NIST
I_np	341.94		NIST
I_np	343.16		NIST
I_np	2098.00		NIST
I_np	2058.00		NIST
I_np	2031.00		NIST
I_np	344.30		NIST
I_np	344.85		NIST
I_np	344.49		NIST
I_np	344.67		NIST
I_np	344.80		NIST
I_np	345.00		NIST
I_np	344.68		NIST
I_np	344.51		NIST
I_np	2020.45		NIST
S°_{solid,1 bar}	230.58	J/mol×K	NIST
T_boil	655.95	K	ChemSep v8.3 pure component data Compiled value
T_c	[905.00; 916.11]	K
T_c	916.11	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
T_c	905.00	K	ChemSep v8.3 pure component data Compiled value
T_fus	[381.00; 386.10]	K
T_fus	382.84	K	Thermodynamic properties of fluoranthene: An experimental and computational study
T_fus	381.50	K	Polar Mixed-Solid Solute Systems in Supercritical Carbon Dioxide: Entrainer Effect and Its Influence on Solubility and Selectivity
T_fus	381.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
T_fus	383.33	K	ChemSep v8.3 pure component data Compiled value
T_fus	381.10	K	Aq. Solubility Prediction
T_fus	381.00 ± 0.20	K	NIST
T_fus	386.10 ± 3.00	K	NIST
T_fus	385.20 ± 3.00	K	NIST
T_fus	385.40 ± 3.00	K	NIST
T_fus	383.45 ± 1.00	K	NIST
T_triple	[383.33; 383.34]	K
T_triple	383.33	K	ChemSep v8.3 pure component data Compiled value
T_triple	383.34 ± 0.01	K	NIST
T_triple	383.33 ± 0.01	K	NIST
T_triple	383.34 ± 0.01	K	NIST
T_triple	383.33 ± 0.01	K	NIST
U_Qi	4.50		ChemSep v8.3 pure component data Compiled value
U_Ri	7.19		ChemSep v8.3 pure component data Compiled value
V_c	[0.655; 0.655]	m³/kmol
V_c	0.655	m³/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
V_c	0.655	m³/kmol	ChemSep v8.3 pure component data Compiled value
Z_c	0.2270000		ChemSep v8.3 pure component data Compiled value
Z_ra	0.23		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,solid	230.25	J/mol×K	298.15	NIST
C_sat	[338.30; 372.10]	J/mol×K	[390.00; 450.00]

C_sat	338.30	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
C_sat	343.90	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
C_sat	349.50	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
C_sat	355.20	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
C_sat	360.80	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
C_sat	366.40	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
C_sat	372.10	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
Δ_fusH	[18.73; 18.74]	kJ/mol	[383.36; 383.40]
Δ_fusH	18.73	kJ/mol	383.36	NIST
Δ_fusH	18.73	kJ/mol	383.36	NIST
Δ_fusH	18.74	kJ/mol	383.40	NIST
Δ_subH	[84.60; 102.60]	kJ/mol	[303.00; 383.00]

Δ_subH	84.60 ± 0.90	kJ/mol	303.00	NIST
Δ_subH	102.60	kJ/mol	328.00	NIST
Δ_subH	102.00 ± 2.00	kJ/mol	340.50	NIST
Δ_subH	102.00 ± 2.00	kJ/mol	340.50	NIST
Δ_subH	98.30	kJ/mol	383.00	NIST
Δ_vapH	[62.20; 101.00]	kJ/mol	[298.15; 580.50]
Δ_vapH	101.00	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
Δ_vapH	79.30	kJ/mol	398.00	NIST
Δ_vapH	77.40	kJ/mol	398.00	NIST
Δ_vapH	62.20	kJ/mol	580.50	NIST
P_sub	[3.96e-05; 1.05e-03]	kPa	[326.80; 359.20]

P_sub	3.96e-05	kPa	326.80	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	4.11e-05	kPa	326.90	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	6.16e-05	kPa	331.00	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	6.32e-05	kPa	331.80	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	1.17e-04	kPa	336.70	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	1.29e-04	kPa	338.70	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	1.31e-04	kPa	338.80	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	1.44e-04	kPa	338.90	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	1.54e-04	kPa	340.20	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	2.06e-04	kPa	342.50	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	2.48e-04	kPa	343.90	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	2.58e-04	kPa	345.30	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	3.30e-04	kPa	348.00	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	3.41e-04	kPa	348.50	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	4.63e-04	kPa	350.90	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	5.80e-04	kPa	354.10	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
P_sub	1.05e-03	kPa	359.20	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Δ_fusS	[48.85; 48.85]	J/mol×K	[383.36; 383.36]
Δ_fusS	48.85	J/mol×K	383.36	NIST
Δ_fusS	48.85	J/mol×K	383.36	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[194.12; 551.81]	J/mol×K	[273.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is C_p,gas in J/mol×K, T in K
Coefficient A			5.99380e+01
Coefficient B			-4.61320e+02
Coefficient C			6.60524e+00
Coefficient D			-5.78100e-05
Coefficient E			-5.67010e-09
Temperature range, min.			273.00
Temperature range, max.			1500.00

C_p,gas	194.12	J/mol×K	273.00	Calculated Property
C_p,gas	293.54	J/mol×K	409.33	Calculated Property
C_p,gas	366.86	J/mol×K	545.67	Calculated Property
C_p,gas	420.17	J/mol×K	682.00	Calculated Property
C_p,gas	459.52	J/mol×K	818.33	Calculated Property
C_p,gas	489.03	J/mol×K	954.67	Calculated Property
C_p,gas	511.44	J/mol×K	1091.00	Calculated Property
C_p,gas	528.60	J/mol×K	1227.33	Calculated Property
C_p,gas	541.76	J/mol×K	1363.67	Calculated Property
C_p,gas	551.81	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[334.56; 381.85]	J/mol×K	[383.33; 450.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is C_p,liquid in J/mol×K, T in K
Coefficient A			2.41580e+02
Coefficient B			1.29690e+03
Coefficient C			-6.12763e+00
Coefficient D			2.34960e-02
Coefficient E			-1.17730e-05
Temperature range, min.			383.33
Temperature range, max.			450.00

C_p,liquid	334.56	J/mol×K	383.33	Calculated Property
C_p,liquid	338.59	J/mol×K	390.74	Calculated Property
C_p,liquid	342.90	J/mol×K	398.15	Calculated Property
C_p,liquid	347.51	J/mol×K	405.55	Calculated Property
C_p,liquid	352.42	J/mol×K	412.96	Calculated Property
C_p,liquid	357.64	J/mol×K	420.37	Calculated Property
C_p,liquid	363.18	J/mol×K	427.78	Calculated Property
C_p,liquid	369.06	J/mol×K	435.18	Calculated Property
C_p,liquid	375.28	J/mol×K	442.59	Calculated Property
C_p,liquid	381.85	J/mol×K	450.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0038101; 0.0002630]	Pa×s	[383.33; 724.00]	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			-6.85020e+01
Coefficient B			5.20890e+03
Coefficient C			8.40070e+00
Coefficient D			-4.29790e-06
Coefficient E			2.00000e+00
Temperature range, min.			383.33
Temperature range, max.			724.00

η	0.0038101	Pa×s	383.33	Calculated Property
η	0.0021742	Pa×s	421.18	Calculated Property
η	0.0014002	Pa×s	459.03	Calculated Property
η	0.0009824	Pa×s	496.89	Calculated Property
η	0.0007328	Pa×s	534.74	Calculated Property
η	0.0005710	Pa×s	572.59	Calculated Property
η	0.0004588	Pa×s	610.44	Calculated Property
η	0.0003765	Pa×s	648.30	Calculated Property
η	0.0003134	Pa×s	686.15	Calculated Property
η	0.0002630	Pa×s	724.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Δ_vapH	[73.34; 0.00]	kJ/mol	[383.33; 905.00]	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 Δ_vapH in kJ/mol, T in K
Coefficient A			1.44268e+02
Coefficient B			2.40371e+00
Coefficient C			-3.37617e+00
Coefficient D			1.40400e+00
Coefficient E			3.27511e-02
Critical temperature, Tc (K)			9.05000e+02
Temperature range, min.			383.33
Temperature range, max.			905.00

Δ_vapH	73.34	kJ/mol	383.33	Calculated Property
Δ_vapH	69.37	kJ/mol	441.29	Calculated Property
Δ_vapH	66.04	kJ/mol	499.26	Calculated Property
Δ_vapH	63.09	kJ/mol	557.22	Calculated Property
Δ_vapH	60.19	kJ/mol	615.18	Calculated Property
Δ_vapH	56.94	kJ/mol	673.15	Calculated Property
Δ_vapH	52.76	kJ/mol	731.11	Calculated Property
Δ_vapH	46.68	kJ/mol	789.07	Calculated Property
Δ_vapH	36.46	kJ/mol	847.04	Calculated Property
Δ_vapH	0.00	kJ/mol	905.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.64]	kPa	[483.47; 698.36]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.59674e+01
Coefficient B			-7.14694e+03
Coefficient C			-2.76650e+01
Temperature range, min.			483.47
Temperature range, max.			698.36

P_vap	1.33	kPa	483.47	Calculated Property
P_vap	2.91	kPa	507.35	Calculated Property
P_vap	5.90	kPa	531.22	Calculated Property
P_vap	11.21	kPa	555.10	Calculated Property
P_vap	20.16	kPa	578.98	Calculated Property
P_vap	34.54	kPa	602.85	Calculated Property
P_vap	56.67	kPa	626.73	Calculated Property
P_vap	89.53	kPa	650.61	Calculated Property
P_vap	136.74	kPa	674.48	Calculated Property
P_vap	202.64	kPa	698.36	Calculated Property
P_vap	[0.02; 2270.35]	kPa	[383.33; 905.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is P_vap in kPa, T in K
Coefficient A			8.92101e+01
Coefficient B			-1.23621e+04
Coefficient C			-1.03511e+01
Coefficient D			3.23190e-06
Coefficient E			2.00000e+00
Temperature range, min.			383.33
Temperature range, max.			905.00

P_vap	0.02	kPa	383.33	Calculated Property
P_vap	0.30	kPa	441.29	Calculated Property
P_vap	2.57	kPa	499.26	Calculated Property
P_vap	13.18	kPa	557.22	Calculated Property
P_vap	47.67	kPa	615.18	Calculated Property
P_vap	134.82	kPa	673.15	Calculated Property
P_vap	319.88	kPa	731.11	Calculated Property
P_vap	668.50	kPa	789.07	Calculated Property
P_vap	1273.95	kPa	847.04	Calculated Property
P_vap	2270.35	kPa	905.00	Calculated Property
P_vap	[0.02; 2603.70]	kPa	[383.15; 905.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is P_vap in kPa, T in K
Coefficient A			1.00473e+02
Coefficient B			-1.29109e+04
Coefficient C			-1.20342e+01
Coefficient D			4.37832e-06
Coefficient E			0.00000e+00
Temperature range, min.			383.15
Temperature range, max.			905.00

P_vap	0.02	kPa	383.15	Calculated Property
P_vap	0.29	kPa	441.13	Calculated Property
P_vap	2.53	kPa	499.12	Calculated Property
P_vap	13.03	kPa	557.10	Calculated Property
P_vap	47.38	kPa	615.08	Calculated Property
P_vap	135.55	kPa	673.07	Calculated Property
P_vap	327.93	kPa	731.05	Calculated Property
P_vap	704.87	kPa	789.03	Calculated Property
P_vap	1394.28	kPa	847.02	Calculated Property
P_vap	2603.70	kPa	905.00	Calculated Property
P_vap	[0.64; 97.87]	kPa	[470.00; 657.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.03896e+01
Coefficient B			-2.34283e+03
Coefficient C			-2.53875e+02
Reference			Tsypkina, 1955
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			470.00
Temperature range, max.			657.40

P_vap	0.64	kPa	470.00	Calculated Property
P_vap	1.65	kPa	490.82	Calculated Property
P_vap	3.67	kPa	511.64	Calculated Property
P_vap	7.24	kPa	532.47	Calculated Property
P_vap	13.00	kPa	553.29	Calculated Property
P_vap	21.62	kPa	574.11	Calculated Property
P_vap	33.79	kPa	594.93	Calculated Property
P_vap	50.18	kPa	615.76	Calculated Property
P_vap	71.36	kPa	636.58	Calculated Property
P_vap	97.87	kPa	657.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρ_l	[1159.60; 308.79]	kg/m³	[298.15; 905.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρ_l in kg/m³, T in K
Coefficient A			7.00920e+01
Coefficient B			2.26990e-01
Coefficient C			9.05000e+02
Coefficient D			2.85080e-01
Temperature range, min.			298.15
Temperature range, max.			905.00

ρ_l	1159.60	kg/m³	298.15	Calculated Property
ρ_l	1110.03	kg/m³	365.58	Calculated Property
ρ_l	1058.22	kg/m³	433.01	Calculated Property
ρ_l	1003.64	kg/m³	500.43	Calculated Property
ρ_l	945.48	kg/m³	567.86	Calculated Property
ρ_l	882.47	kg/m³	635.29	Calculated Property
ρ_l	812.44	kg/m³	702.72	Calculated Property
ρ_l	731.02	kg/m³	770.14	Calculated Property
ρ_l	626.36	kg/m³	837.57	Calculated Property
ρ_l	308.79	kg/m³	905.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 1.44e-05]	N/m	[383.33; 899.78]	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			-8.10350e-03
Coefficient B			3.09570e+02
Coefficient C			-4.48530e+00
Coefficient D			3.18680e-03
Coefficient E			-4.37230e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 905 K.
Temperature range, min.			383.33
Temperature range, max.			899.78

γ	0.04	N/m	383.33	Calculated Property
γ	0.03	N/m	440.71	Calculated Property
γ	0.03	N/m	498.10	Calculated Property
γ	0.02	N/m	555.48	Calculated Property
γ	0.02	N/m	612.86	Calculated Property
γ	0.01	N/m	670.25	Calculated Property
γ	0.01	N/m	727.63	Calculated Property
γ	0.01	N/m	785.02	Calculated Property
γ	0.00	N/m	842.40	Calculated Property
γ	1.44e-05	N/m	899.78	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_gas	[0.01; 0.05]	W/m×K	[383.33; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ_gas in W/m×K, T in K
Coefficient A			1.17760e-04
Coefficient B			9.47880e-01
Coefficient C			6.60840e+02
Coefficient D			3.82920e+04
Temperature range, min.			383.33
Temperature range, max.			1000.00

λ_gas	0.01	W/m×K	383.33	Calculated Property
λ_gas	0.01	W/m×K	451.85	Calculated Property
λ_gas	0.02	W/m×K	520.37	Calculated Property
λ_gas	0.02	W/m×K	588.89	Calculated Property
λ_gas	0.03	W/m×K	657.41	Calculated Property
λ_gas	0.03	W/m×K	725.92	Calculated Property
λ_gas	0.03	W/m×K	794.44	Calculated Property
λ_gas	0.04	W/m×K	862.96	Calculated Property
λ_gas	0.04	W/m×K	931.48	Calculated Property
λ_gas	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_liquid	[0.14; 0.10]	W/m×K	[383.33; 655.95]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ_liquid in W/m×K, T in K
Coefficient A			-4.58640e-02
Coefficient B			-8.33970e+01
Coefficient C			-9.60490e-01
Coefficient D			-1.32190e-03
Coefficient E			-5.13550e-10
Temperature range, min.			383.33
Temperature range, max.			655.95

λ_liquid	0.14	W/m×K	383.33	Calculated Property
λ_liquid	0.14	W/m×K	413.62	Calculated Property
λ_liquid	0.13	W/m×K	443.91	Calculated Property
λ_liquid	0.13	W/m×K	474.20	Calculated Property
λ_liquid	0.12	W/m×K	504.49	Calculated Property
λ_liquid	0.12	W/m×K	534.79	Calculated Property
λ_liquid	0.11	W/m×K	565.08	Calculated Property
λ_liquid	0.11	W/m×K	595.37	Calculated Property
λ_liquid	0.10	W/m×K	625.66	Calculated Property
λ_liquid	0.10	W/m×K	655.95	Calculated Property

Similar Compounds

Find more compounds similar to Fluoranthene.

Mixtures

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
Thermodynamic properties of fluoranthene: An experimental and computational study
Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
Solution calorimetry as a complementary tool for the determination of enthalpies of vaporization and sublimation of low volatile compounds at 298.15 K
Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
Enthalpies of solution, enthalpies of fusion and enthalpies of solvation of polyaromatic hydrocarbons: Instruments for determination of sublimation enthalpy at 298.15 K
Ionic Liquids/Water Distribution Ratios of Some Polycyclic Aromatic Hydrocarbons
Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
Polar Mixed-Solid Solute Systems in Supercritical Carbon Dioxide: Entrainer Effect and Its Influence on Solubility and Selectivity
Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.

Chemical Properties of Fluoranthene (CAS 206-44-0)