Chemical Properties of Acenaphthene (CAS 83-32-9)

InChI

InChI=1S/C12H10/c1-3-9-4-2-6-11-8-7-10(5-1)12(9)11/h1-6H,7-8H2

InChI Key

CWRYPZZKDGJXCA-UHFFFAOYSA-N

Formula

C12H10

SMILES

c1cc2c3c(cccc3c1)CC2

Molecular Weight¹

154.21

CAS

83-32-9

Other Names

• 1,2-DIHYDRO-ACENAPHTHYLENE
• 1,2-dihydroacenaphthylene
• 1,8-Ethylenenaphthalene
• Acenaphthylene, 1,2-dihydro-
• Acenapthene
• Naphthyleneethylene
• Peri-Ethylenenaphthalene
• acenaphtene

• 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).
• 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.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3811		ChemSep v8.3 pure component data Compiled value
PAff	[849.80; 851.70]	kJ/mol
PAff	851.70	kJ/mol	NIST
PAff	849.80	kJ/mol	NIST
BasG	[821.00; 821.70]	kJ/mol
BasG	821.00	kJ/mol	NIST
BasG	821.70	kJ/mol	NIST
ΔcH°solid	-6222.00 ± 3.00	kJ/mol	NIST
μ	0.25	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	260.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[155.00; 156.80]	kJ/mol
ΔfH°gas	155.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	156.80 ± 3.10	kJ/mol	NIST
ΔfH°gas	156.00 ± 4.00	kJ/mol	NIST
ΔfH°solid	[70.00; 72.00]	kJ/mol
ΔfH°solid	72.00 ± 3.10	kJ/mol	NIST
ΔfH°solid	70.00 ± 3.00	kJ/mol	NIST
ΔfusH°	16.28	kJ/mol	Joback Calculated Property
ΔsubH°	[83.40; 86.00]	kJ/mol
ΔsubH°	84.80 ± 0.40	kJ/mol	NIST
ΔsubH°	84.60	kJ/mol	NIST
ΔsubH°	83.40 ± 1.00	kJ/mol	NIST
ΔsubH°	86.00 ± 1.00	kJ/mol	NIST
ΔsubH°	86.00	kJ/mol	NIST
ΔsubH°	83.40 ± 1.00	kJ/mol	NIST
ΔvapH°	[66.20; 70.50]	kJ/mol
ΔvapH°	68.00	kJ/mol	NIST
ΔvapH°	70.50 ± 1.10	kJ/mol	NIST
ΔvapH°	66.20	kJ/mol	NIST
ΔvapH°	66.20	kJ/mol	NIST
ΔvapH°	66.50 ± 1.30	kJ/mol	NIST
IE	[7.66; 7.82]	eV
IE	7.75 ± 0.05	eV	NIST
IE	7.68 ± 0.05	eV	NIST
IE	7.73 ± 0.01	eV	NIST
IE	7.66	eV	NIST
IE	7.76 ± 0.03	eV	NIST
IE	7.82 ± 0.04	eV	NIST
log10WS	[-4.63; -4.58]
log10WS	-4.58		Aq. Solubility Prediction
log10WS	-4.63		Estimated Solubility
log10WS	-4.59		Rytting (2005)
logPoct/wat	2.938		Crippen Calculated Property
McVol	125.860	ml/mol	McGowan Calculated Property
Pc	3100.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	0.20	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[231.65; 1526.00]
Inp	1472.00		NIST
Inp	1472.00		NIST
Inp	1475.00		NIST
Inp	1486.00		NIST
Inp	1463.90		NIST
Inp	1475.00		NIST
Inp	1481.40		NIST
Inp	1480.50		NIST
Inp	1468.00		NIST
Inp	1481.40		NIST
Inp	1488.60		NIST
Inp	1468.00		NIST
Inp	1481.40		NIST
Inp	1488.60		NIST
Inp	1481.40		NIST
Inp	1480.50		NIST
Inp	1445.50		NIST
Inp	1445.30		NIST
Inp	1493.00		NIST
Inp	1456.00		NIST
Inp	1481.00		NIST
Inp	1461.00		NIST
Inp	1458.00		NIST
Inp	1455.06		NIST
Inp	1488.20		NIST
Inp	1503.00		NIST
Inp	1439.00		NIST
Inp	1472.00		NIST
Inp	1450.00		NIST
Inp	1464.00		NIST
Inp	1455.00		NIST
Inp	1458.00		NIST
Inp	1466.00		NIST
Inp	1472.00		NIST
Inp	1518.00		NIST
Inp	1520.00		NIST
Inp	1523.00		NIST
Inp	1523.00		NIST
Inp	1523.00		NIST
Inp	1523.00		NIST
Inp	1523.00		NIST
Inp	1523.00		NIST
Inp	1523.00		NIST
Inp	1523.00		NIST
Inp	1525.00		NIST
Inp	1526.00		NIST
Inp	1496.00		NIST
Inp	1503.00		NIST
Inp	1492.00		NIST
Inp	1494.00		NIST
Inp	1483.00		NIST
Inp	1483.00		NIST
Inp	1485.00		NIST
Inp	1485.00		NIST
Inp	1485.00		NIST
Inp	1486.00		NIST
Inp	1491.00		NIST
Inp	1491.00		NIST
Inp	1460.00		NIST
Inp	1437.00		NIST
Inp	1474.00		NIST
Inp	1457.00		NIST
Inp	1476.00		NIST
Inp	1447.00		NIST
Inp	1446.00		NIST
Inp	1463.00		NIST
Inp	1494.00		NIST
Inp	1494.00		NIST
Inp	1522.00		NIST
Inp	254.40		NIST
Inp	242.90		NIST
Inp	243.10		NIST
Inp	251.29		NIST
Inp	253.30		NIST
Inp	254.07		NIST
Inp	243.16		NIST
Inp	243.16		NIST
Inp	254.87		NIST
Inp	254.36		NIST
Inp	254.04		NIST
Inp	254.10		NIST
Inp	254.21		NIST
Inp	254.30		NIST
Inp	254.33		NIST
Inp	254.60		NIST
Inp	254.83		NIST
Inp	254.89		NIST
Inp	254.91		NIST
Inp	253.90		NIST
Inp	254.30		NIST
Inp	253.54		NIST
Inp	253.91		NIST
Inp	254.80		NIST
Inp	253.71		NIST
Inp	253.67		NIST
Inp	254.98		NIST
Inp	231.65		NIST
Inp	253.14		NIST
Inp	251.29		NIST
Inp	255.00		NIST
Inp	253.56		NIST
Inp	253.56		NIST
Inp	253.67		NIST
Inp	254.50		NIST
Inp	251.99		NIST
Inp	245.85		NIST
Inp	245.90		NIST
Inp	251.30		NIST
Inp	253.30		NIST
Inp	253.50		NIST
Inp	253.30		NIST
Inp	245.85		NIST
Inp	245.90		NIST
Inp	257.17		NIST
Inp	255.60		NIST
Inp	253.50		NIST
Inp	247.80		NIST
Inp	1464.00		NIST
Inp	1481.40		NIST
Inp	1468.00		NIST
Inp	1445.50		NIST
Inp	1461.00		NIST
Inp	1455.06		NIST
Inp	1450.00		NIST
Inp	254.40		NIST
Inp	254.07		NIST
Inp	254.04		NIST
Inp	254.60		NIST
Inp	254.30		NIST
Inp	253.67		NIST
Inp	1457.00		NIST
Inp	1494.00		NIST
Inp	1472.00		NIST
Inp	1523.00		NIST
Inp	1492.00		NIST
Inp	1485.00		NIST
Inp	1460.00		NIST
Ip	[2092.00; 2133.00]
Ip	2132.00		NIST
Ip	2108.00		NIST
Ip	2133.00		NIST
Ip	2092.00		NIST
Ip	2103.00		NIST
S°solid,1 bar	188.87	J/mol×K	NIST
Tboil	[502.65; 552.20]	K
Tboil	550.54	K	ChemSep v8.3 pure component data Compiled value
Tboil	552.20	K	NIST
Tboil	552.00	K	NIST
Tboil	502.65 ± 1.00	K	NIST
Tc	[803.15; 820.00]	K
Tc	820.00	K	Critical point measurement of some polycyclic aromatic hydrocarbons
Tc	803.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	[363.00; 370.00]	K
Tfus	368.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	366.56	K	ChemSep v8.3 pure component data Compiled value
Tfus	367.55	K	Aq. Solubility Prediction
Tfus	364.02 ± 0.20	K	NIST
Tfus	369.00	K	NIST
Tfus	366.50 ± 0.20	K	NIST
Tfus	363.10 ± 1.00	K	NIST
Tfus	366.40 ± 0.20	K	NIST
Tfus	367.20 ± 3.00	K	NIST
Tfus	370.00 ± 1.50	K	NIST
Tfus	367.65 ± 1.00	K	NIST
Tfus	363.00 ± 1.00	K	NIST
Tfus	368.35 ± 0.50	K	NIST
Tfus	367.80 ± 0.20	K	NIST
Tfus	366.00 ± 0.20	K	NIST
Tfus	367.25 ± 0.50	K	NIST
Ttriple	[366.55; 366.56]	K
Ttriple	366.56	K	ChemSep v8.3 pure component data Compiled value
Ttriple	366.56 ± 0.02	K	NIST
Ttriple	366.55 ± 0.02	K	NIST
Ttriple	366.56 ± 0.02	K	NIST
UQi	3.96		ChemSep v8.3 pure component data Compiled value
URi	6.00		ChemSep v8.3 pure component data Compiled value
Vc	0.553	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2570000		ChemSep v8.3 pure component data Compiled value
Zra	0.24		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,solid	[185.80; 210.50]	J/mol×K	[298.00; 298.15]
Cp,solid	185.80	J/mol×K	298.00	NIST
Cp,solid	210.50	J/mol×K	298.10	NIST
Cp,solid	190.37	J/mol×K	298.15	NIST
Csat	[268.90; 287.80]	J/mol×K	[380.00; 420.00]
Csat	268.90	J/mol×K	380.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	273.60	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
Csat	278.30	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
Csat	283.10	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
Csat	287.80	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
ΔfusH	[20.23; 25.10]	kJ/mol	[366.40; 367.80]
ΔfusH	20.23	kJ/mol	366.40	NIST
ΔfusH	21.46	kJ/mol	366.56	NIST
ΔfusH	21.46	kJ/mol	366.56	NIST
ΔfusH	21.46	kJ/mol	366.60	NIST
ΔfusH	21.46	kJ/mol	366.60	NIST
ΔfusH	21.00	kJ/mol	367.00	NIST
ΔfusH	25.10	kJ/mol	367.80	NIST
ΔsubH	[77.00; 86.80]	kJ/mol	[283.00; 383.00]
ΔsubH	84.70 ± 2.70	kJ/mol	283.00	NIST
ΔsubH	81.60	kJ/mol	283.00	NIST
ΔsubH	82.10 ± 0.40	kJ/mol	300.50	NIST
ΔsubH	86.80 ± 0.90	kJ/mol	303.00	NIST
ΔsubH	86.20 ± 0.80	kJ/mol	315.00	NIST
ΔsubH	77.00	kJ/mol	317.50	NIST
ΔsubH	82.40	kJ/mol	366.00	NIST
ΔsubH	82.13 ± 0.42	kJ/mol	368.00	NIST
ΔsubH	83.20	kJ/mol	383.00	NIST
ΔvapH	[54.00; 67.98]	kJ/mol	[298.00; 490.50]
ΔvapH	67.98	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH	61.10	kJ/mol	366.00	NIST
ΔvapH	60.60	kJ/mol	378.00	NIST
ΔvapH	60.30	kJ/mol	390.50	NIST
ΔvapH	61.30	kJ/mol	395.00	NIST
ΔvapH	63.90	kJ/mol	398.00	NIST
ΔvapH	54.00	kJ/mol	460.00	NIST
ΔvapH	54.30	kJ/mol	487.00	NIST
ΔvapH	55.40	kJ/mol	490.50	NIST
Psub	[2.90e-04; 1.80e-03]	kPa	[297.60; 315.60]
Psub	2.90e-04	kPa	297.60	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	3.62e-04	kPa	299.70	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	4.13e-04	kPa	300.50	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	4.40e-04	kPa	301.60	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	5.08e-04	kPa	302.80	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	6.93e-04	kPa	306.10	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	1.12e-03	kPa	310.70	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
Psub	1.80e-03	kPa	315.60	Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
ΔfusS	[55.22; 68.20]	J/mol×K	[366.40; 367.80]
ΔfusS	55.22	J/mol×K	366.40	NIST
ΔfusS	58.55	J/mol×K	366.56	NIST
ΔfusS	58.55	J/mol×K	366.56	NIST
ΔfusS	68.20	J/mol×K	367.80	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[106.21; 461.22]	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			6.07620e+01
Coefficient B			-5.15400e+02
Coefficient C			6.39924e+00
Coefficient D			-2.68230e-05
Coefficient E			-1.01300e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	106.21	J/mol×K	200.00	Calculated Property
Cp,gas	194.05	J/mol×K	344.44	Calculated Property
Cp,gas	267.09	J/mol×K	488.89	Calculated Property
Cp,gas	321.73	J/mol×K	633.33	Calculated Property
Cp,gas	362.51	J/mol×K	777.78	Calculated Property
Cp,gas	393.39	J/mol×K	922.22	Calculated Property
Cp,gas	417.11	J/mol×K	1066.67	Calculated Property
Cp,gas	435.54	J/mol×K	1211.11	Calculated Property
Cp,gas	449.95	J/mol×K	1355.56	Calculated Property
Cp,gas	461.22	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[265.04; 351.60]	J/mol×K	[366.56; 550.54]	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			1.73930e+02
Coefficient B			3.79650e+02
Coefficient C			-1.27856e+00
Coefficient D			1.79390e-02
Coefficient E			-1.35510e-05
Temperature range, min.			366.56
Temperature range, max.			550.54
Cp,liquid	265.04	J/mol×K	366.56	Calculated Property
Cp,liquid	274.95	J/mol×K	387.00	Calculated Property
Cp,liquid	285.29	J/mol×K	407.44	Calculated Property
Cp,liquid	295.87	J/mol×K	427.89	Calculated Property
Cp,liquid	306.50	J/mol×K	448.33	Calculated Property
Cp,liquid	316.93	J/mol×K	468.77	Calculated Property
Cp,liquid	326.91	J/mol×K	489.21	Calculated Property
Cp,liquid	336.19	J/mol×K	509.66	Calculated Property
Cp,liquid	344.51	J/mol×K	530.10	Calculated Property
Cp,liquid	351.60	J/mol×K	550.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0015279; 0.0002112]	Pa×s	[366.56; 550.54]	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			-8.20730e+00
Coefficient B			1.37320e+03
Coefficient C			-2.58710e-01
Coefficient D			-3.68590e-06
Coefficient E			2.00000e+00
Temperature range, min.			366.56
Temperature range, max.			550.54
η	0.0015279	Pa×s	366.56	Calculated Property
η	0.0011679	Pa×s	387.00	Calculated Property
η	0.0009085	Pa×s	407.44	Calculated Property
η	0.0007170	Pa×s	427.89	Calculated Property
η	0.0005729	Pa×s	448.33	Calculated Property
η	0.0004624	Pa×s	468.77	Calculated Property
η	0.0003765	Pa×s	489.21	Calculated Property
η	0.0003087	Pa×s	509.66	Calculated Property
η	0.0002547	Pa×s	530.10	Calculated Property
η	0.0002112	Pa×s	550.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[60.15; 0.00]	kJ/mol	[366.56; 803.15]	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			3.78598e+02
Coefficient B			1.01448e+01
Coefficient C			-2.54194e+01
Coefficient D			2.60377e+01
Coefficient E			-9.98216e+00
Critical temperature, Tc (K)			8.03150e+02
Temperature range, min.			366.56
Temperature range, max.			803.15
ΔvapH	60.15	kJ/mol	366.56	Calculated Property
ΔvapH	57.78	kJ/mol	415.07	Calculated Property
ΔvapH	55.62	kJ/mol	463.58	Calculated Property
ΔvapH	53.10	kJ/mol	512.09	Calculated Property
ΔvapH	49.86	kJ/mol	560.60	Calculated Property
ΔvapH	45.69	kJ/mol	609.11	Calculated Property
ΔvapH	40.51	kJ/mol	657.62	Calculated Property
ΔvapH	34.09	kJ/mol	706.13	Calculated Property
ΔvapH	25.04	kJ/mol	754.64	Calculated Property
ΔvapH	0.00	kJ/mol	803.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.68]	kPa	[405.49; 502.35]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			2.24317e+01
Coefficient B			-7.30879e+03
Coefficient C			-7.54360e+01
Temperature range, min.			405.49
Temperature range, max.			502.35
Pvap	1.33	kPa	405.49	Calculated Property
Pvap	2.68	kPa	416.25	Calculated Property
Pvap	5.17	kPa	427.01	Calculated Property
Pvap	9.59	kPa	437.78	Calculated Property
Pvap	17.16	kPa	448.54	Calculated Property
Pvap	29.72	kPa	459.30	Calculated Property
Pvap	49.95	kPa	470.06	Calculated Property
Pvap	81.66	kPa	480.83	Calculated Property
Pvap	130.17	kPa	491.59	Calculated Property
Pvap	202.68	kPa	502.35	Calculated Property
Pvap	[0.16; 3107.05]	kPa	[363.15; 803.15]	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			6.68292e+01
Coefficient B			-9.73550e+03
Coefficient C			-7.13210e+00
Coefficient D			1.60790e-06
Coefficient E			2.00000e+00
Temperature range, min.			363.15
Temperature range, max.			803.15
Pvap	0.16	kPa	363.15	Calculated Property
Pvap	1.70	kPa	412.04	Calculated Property
Pvap	10.04	kPa	460.93	Calculated Property
Pvap	40.01	kPa	509.82	Calculated Property
Pvap	120.43	kPa	558.71	Calculated Property
Pvap	294.88	kPa	607.59	Calculated Property
Pvap	618.46	kPa	656.48	Calculated Property
Pvap	1152.67	kPa	705.37	Calculated Property
Pvap	1961.04	kPa	754.26	Calculated Property
Pvap	3107.05	kPa	803.15	Calculated Property
Pvap	[0.20; 3117.44]	kPa	[366.15; 803.15]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			6.77558e+01
Coefficient B			-9.75784e+03
Coefficient C			-7.27940e+00
Coefficient D			1.74725e-06
Coefficient E			0.00000e+00
Temperature range, min.			366.15
Temperature range, max.			803.15
Pvap	0.20	kPa	366.15	Calculated Property
Pvap	1.91	kPa	414.71	Calculated Property
Pvap	10.85	kPa	463.26	Calculated Property
Pvap	42.08	kPa	511.82	Calculated Property
Pvap	124.32	kPa	560.37	Calculated Property
Pvap	300.56	kPa	608.93	Calculated Property
Pvap	625.18	kPa	657.48	Calculated Property
Pvap	1159.47	kPa	706.04	Calculated Property
Pvap	1968.02	kPa	754.59	Calculated Property
Pvap	3117.44	kPa	803.15	Calculated Property
Pvap	[0.21; 1.80]	kPa	[368.00; 413.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45578e+01
Coefficient B			-4.74816e+03
Coefficient C			-7.31460e+01
Reference			Osborn and Douslin, 1975, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			368.00
Temperature range, max.			413.00
Pvap	0.21	kPa	368.00	Calculated Property
Pvap	0.28	kPa	373.00	Calculated Property
Pvap	0.36	kPa	378.00	Calculated Property
Pvap	0.46	kPa	383.00	Calculated Property
Pvap	0.59	kPa	388.00	Calculated Property
Pvap	0.75	kPa	393.00	Calculated Property
Pvap	0.94	kPa	398.00	Calculated Property
Pvap	1.18	kPa	403.00	Calculated Property
Pvap	1.46	kPa	408.00	Calculated Property
Pvap	1.80	kPa	413.00	Calculated Property
Pvap	[2.55; 126.32]	kPa	[420.40; 560.90]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.59596e+01
Coefficient B			-6.01272e+03
Coefficient C			-2.02270e+01
Reference			Mortimer and Murphy, 1923
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			420.40
Temperature range, max.			560.90
Pvap	2.55	kPa	420.40	Calculated Property
Pvap	4.47	kPa	436.01	Calculated Property
Pvap	7.55	kPa	451.62	Calculated Property
Pvap	12.29	kPa	467.23	Calculated Property
Pvap	19.35	kPa	482.84	Calculated Property
Pvap	29.57	kPa	498.46	Calculated Property
Pvap	44.00	kPa	514.07	Calculated Property
Pvap	63.90	kPa	529.68	Calculated Property
Pvap	90.75	kPa	545.29	Calculated Property
Pvap	126.32	kPa	560.90	Calculated Property
Pvap	[0.21; 1.80]	kPa	[368.00; 413.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45578e+01
Coefficient B			-4.74816e+03
Coefficient C			-7.31460e+01
Reference			Osborn and Douslin, 1975
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			368.00
Temperature range, max.			413.00
Pvap	0.21	kPa	368.00	Calculated Property
Pvap	0.28	kPa	373.00	Calculated Property
Pvap	0.36	kPa	378.00	Calculated Property
Pvap	0.46	kPa	383.00	Calculated Property
Pvap	0.59	kPa	388.00	Calculated Property
Pvap	0.75	kPa	393.00	Calculated Property
Pvap	0.94	kPa	398.00	Calculated Property
Pvap	1.18	kPa	403.00	Calculated Property
Pvap	1.46	kPa	408.00	Calculated Property
Pvap	1.80	kPa	413.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1029.50; 279.13]	kg/m3	[366.56; 803.15]	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			6.15937e+01
Coefficient B			2.20660e-01
Coefficient C			8.03150e+02
Coefficient D			2.40430e-01
Temperature range, min.			366.56
Temperature range, max.			803.15
ρl	1029.50	kg/m3	366.56	Calculated Property
ρl	992.66	kg/m3	415.07	Calculated Property
ρl	953.65	kg/m3	463.58	Calculated Property
ρl	911.96	kg/m3	512.09	Calculated Property
ρl	866.81	kg/m3	560.60	Calculated Property
ρl	816.99	kg/m3	609.11	Calculated Property
ρl	760.41	kg/m3	657.62	Calculated Property
ρl	692.82	kg/m3	706.13	Calculated Property
ρl	602.58	kg/m3	754.64	Calculated Property
ρl	279.13	kg/m3	803.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 5.65e-06]	N/m	[366.56; 799.66]	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			-9.09140e-03
Coefficient B			2.66350e+02
Coefficient C			-4.47640e+00
Coefficient D			3.72620e-03
Coefficient E			-5.53000e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 803.15 K.
Temperature range, min.			366.56
Temperature range, max.			799.66
γ	0.03	N/m	366.56	Calculated Property
γ	0.03	N/m	414.68	Calculated Property
γ	0.03	N/m	462.80	Calculated Property
γ	0.02	N/m	510.93	Calculated Property
γ	0.02	N/m	559.05	Calculated Property
γ	0.01	N/m	607.17	Calculated Property
γ	0.01	N/m	655.29	Calculated Property
γ	0.01	N/m	703.41	Calculated Property
γ	0.00	N/m	751.54	Calculated Property
γ	5.65e-06	N/m	799.66	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.06]	W/m×K	[366.56; 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			7.80270e-05
Coefficient B			1.02860e+00
Coefficient C			5.93390e+02
Coefficient D			3.76220e+04
Temperature range, min.			366.56
Temperature range, max.			1000.00
λgas	0.01	W/m×K	366.56	Calculated Property
λgas	0.02	W/m×K	436.94	Calculated Property
λgas	0.02	W/m×K	507.32	Calculated Property
λgas	0.03	W/m×K	577.71	Calculated Property
λgas	0.03	W/m×K	648.09	Calculated Property
λgas	0.04	W/m×K	718.47	Calculated Property
λgas	0.04	W/m×K	788.85	Calculated Property
λgas	0.05	W/m×K	859.24	Calculated Property
λgas	0.05	W/m×K	929.62	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.13; 0.11]	W/m×K	[366.56; 550.54]	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			5.95520e-02
Coefficient B			-9.15920e+01
Coefficient C			-1.71690e+00
Coefficient D			-1.90560e-03
Coefficient E			1.29510e-07
Temperature range, min.			366.56
Temperature range, max.			550.54
λliquid	0.13	W/m×K	366.56	Calculated Property
λliquid	0.13	W/m×K	387.00	Calculated Property
λliquid	0.13	W/m×K	407.44	Calculated Property
λliquid	0.13	W/m×K	427.89	Calculated Property
λliquid	0.12	W/m×K	448.33	Calculated Property
λliquid	0.12	W/m×K	468.77	Calculated Property
λliquid	0.12	W/m×K	489.21	Calculated Property
λliquid	0.12	W/m×K	509.66	Calculated Property
λliquid	0.12	W/m×K	530.10	Calculated Property
λliquid	0.11	W/m×K	550.54	Calculated Property

Similar Compounds

Find more compounds similar to Acenaphthene.

Mixtures

• Acenaphthene + Carbazole
• Anthracene + Acenaphthene
• 9H-Fluoren-9-one + Acenaphthene
• Ethanol + Acenaphthene
• Ethanol + 9H-Fluoren-9-one + Acenaphthene
• Acenaphthene + Water
• Acenaphthene + Acetone
• Acenaphthene + 1-Propanol, 2-methyl-
• Benzene + Acenaphthene
• Acenaphthene + Benzene, 1,3-dimethyl-
• 1-Propanol + Acenaphthene

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).
• 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
• 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
• New aspects of relationship between the enthalpies of fusion of aromatic compounds at the melting temperatures and the enthalpies of solution in benzene at 298.15 K. Part I
• Solubility of Acenaphthene, Anthracene, and Pyrene in Water At 50 C to 300 C
• 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
• Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Solubility of Acenaphthene in Different Solvents from (283.00 to 323.00) 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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