Chemical Properties of Anthracene (CAS 120-12-7)

InChI

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

InChI Key

MWPLVEDNUUSJAV-UHFFFAOYSA-N

Formula

C14H10

SMILES

c1ccc2cc3ccccc3cc2c1

Molecular Weight¹

178.23

CAS

120-12-7

Other Names

• Anthracen
• Anthracene oil
• Anthracin
• Coal tar pitch volatiles:anthracene
• GREENOIL
• Green Oil
• Paranaphthalene
• Sterilite hop defoliant
• Tetra Olive N2G
• p-Naphthalene

• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• C_p,gas : Ideal gas 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_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 a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_sub : Sublimation pressure (kPa).
• P_vap : Vapor pressure (kPa).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• 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).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
PAff	[869.40; 877.30]	kJ/mol
PAff	877.30	kJ/mol	NIST
PAff	869.40	kJ/mol	NIST
Tig	813.15	K	KDB
BasG	[842.70; 846.60]	kJ/mol
BasG	846.60	kJ/mol	NIST
BasG	842.70	kJ/mol	NIST
μ	0.00	debye	KDB
EA	[0.42; 0.66]	eV
EA	0.53 ± 0.02	eV	NIST
EA	0.53 ± 0.01	eV	NIST
EA	0.60 ± 0.10	eV	NIST
EA	0.66 ± 0.06	eV	NIST
EA	0.57 ± 0.02	eV	NIST
EA	0.56 ± 0.01	eV	NIST
EA	0.48 ± 0.04	eV	NIST
EA	0.42	eV	NIST
ΔfG°	383.08	kJ/mol	Joback Calculated Property
ΔfH°gas	224.80	kJ/mol	KDB
ΔfusH°	[27.39; 101.80]	kJ/mol
ΔfusH°	101.80	kJ/mol	New Knu...
ΔfusH°	100.60	kJ/mol	New Knu...
ΔfusH°	27.39	kJ/mol	Thermod...
ΔvapH°	[78.50; 79.80]	kJ/mol
ΔvapH°	78.50	kJ/mol	NIST
ΔvapH°	79.50 ± 1.20	kJ/mol	NIST
ΔvapH°	79.10	kJ/mol	NIST
ΔvapH°	79.80	kJ/mol	NIST
ΔvapH°	79.60	kJ/mol	NIST
IE	[7.15; 21.10]	eV
IE	7.44 ± 0.01	eV	NIST
IE	7.44 ± 0.01	eV	NIST
IE	7.47	eV	NIST
IE	7.43	eV	NIST
IE	7.45 ± 0.05	eV	NIST
IE	7.47	eV	NIST
IE	7.47	eV	NIST
IE	7.40	eV	NIST
IE	7.41 ± 0.05	eV	NIST
IE	7.47 ± 0.01	eV	NIST
IE	7.40	eV	NIST
IE	7.47 ± 0.01	eV	NIST
IE	7.41	eV	NIST
IE	7.41	eV	NIST
IE	7.50	eV	NIST
IE	7.15	eV	NIST
IE	7.42	eV	NIST
IE	7.20	eV	NIST
IE	7.43	eV	NIST
IE	7.40	eV	NIST
IE	7.40	eV	NIST
IE	7.35	eV	NIST
IE	7.37	eV	NIST
IE	7.55	eV	NIST
IE	Outlier 21.10	eV	NIST
IE	7.40	eV	NIST
IE	7.40	eV	NIST
IE	7.23	eV	NIST
IE	7.43 ± 0.03	eV	NIST
IE	7.41 ± 0.02	eV	NIST
IE	7.41	eV	NIST
IE	7.40	eV	NIST
IE	7.42 ± 0.02	eV	NIST
IE	7.44 ± 0.03	eV	NIST
IE	7.40	eV	NIST
log10WS	[-6.44; -6.35]
log10WS	-6.44		Aq. Sol...
log10WS	-6.35		Estimat...
logPoct/wat	3.993		Crippen Calculated Property
McVol	145.440	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
Pc	3243.03	kPa	Joback Calculated Property
Inp	[300.00; 1817.00]
Inp	1804.00		NIST
Inp	1739.00		NIST
Inp	1752.00		NIST
Inp	1769.00		NIST
Inp	1729.00		NIST
Inp	1767.00		NIST
Inp	1786.40		NIST
Inp	1800.00		NIST
Inp	1780.10		NIST
Inp	1800.10		NIST
Inp	1770.90		NIST
Inp	1767.00		NIST
Inp	1786.40		NIST
Inp	1800.00		NIST
Inp	1759.49		NIST
Inp	1764.27		NIST
Inp	1770.93		NIST
Inp	1781.68		NIST
Inp	1779.87		NIST
Inp	1791.49		NIST
Inp	1782.28		NIST
Inp	1806.00		NIST
Inp	1751.95		NIST
Inp	1757.74		NIST
Inp	1758.00		NIST
Inp	1757.98		NIST
Inp	1752.00		NIST
Inp	1740.00		NIST
Inp	1749.00		NIST
Inp	1749.00		NIST
Inp	1749.00		NIST
Inp	1749.00		NIST
Inp	1750.00		NIST
Inp	1762.00		NIST
Inp	1762.00		NIST
Inp	1762.00		NIST
Inp	1762.00		NIST
Inp	1764.00		NIST
Inp	1765.00		NIST
Inp	1766.00		NIST
Inp	1770.00		NIST
Inp	1773.00		NIST
Inp	1778.00		NIST
Inp	1754.20		NIST
Inp	1744.40		NIST
Inp	1750.00		NIST
Inp	1754.97		NIST
Inp	1793.42		NIST
Inp	1734.00		NIST
Inp	1771.00		NIST
Inp	1733.00		NIST
Inp	1759.00		NIST
Inp	1734.00		NIST
Inp	1729.00		NIST
Inp	1759.00		NIST
Inp	1759.00		NIST
Inp	1763.00		NIST
Inp	1775.00		NIST
Inp	1817.00		NIST
Inp	1812.00		NIST
Inp	1785.00		NIST
Inp	1786.00		NIST
Inp	1788.00		NIST
Inp	1789.00		NIST
Inp	1790.00		NIST
Inp	1791.00		NIST
Inp	1801.00		NIST
Inp	1802.00		NIST
Inp	1762.00		NIST
Inp	1754.00		NIST
Inp	1753.00		NIST
Inp	1725.00		NIST
Inp	1743.00		NIST
Inp	1723.00		NIST
Inp	1777.00		NIST
Inp	1789.00		NIST
Inp	1791.00		NIST
Inp	1793.00		NIST
Inp	1797.00		NIST
Inp	1766.00		NIST
Inp	1742.00		NIST
Inp	1724.00		NIST
Inp	1752.00		NIST
Inp	1750.00		NIST
Inp	1758.00		NIST
Inp	1766.00		NIST
Inp	1754.00		NIST
Inp	300.00		NIST
Inp	300.00		NIST
Inp	300.00		NIST
Inp	300.65		NIST
Inp	300.00		NIST
Inp	301.40		NIST
Inp	301.30		NIST
Inp	301.40		NIST
Inp	301.69		NIST
Inp	301.40		NIST
Inp	301.68		NIST
Inp	301.38		NIST
Inp	301.38		NIST
Inp	301.84		NIST
Inp	301.59		NIST
Inp	301.41		NIST
Inp	301.65		NIST
Inp	301.65		NIST
Inp	301.67		NIST
Inp	301.68		NIST
Inp	301.68		NIST
Inp	301.68		NIST
Inp	301.69		NIST
Inp	301.69		NIST
Inp	301.25		NIST
Inp	301.67		NIST
Inp	301.70		NIST
Inp	301.70		NIST
Inp	301.61		NIST
Inp	301.48		NIST
Inp	301.35		NIST
Inp	301.24		NIST
Inp	301.61		NIST
Inp	301.54		NIST
Inp	301.33		NIST
Inp	301.76		NIST
Inp	301.60		NIST
Inp	301.50		NIST
Inp	302.00		NIST
Inp	301.16		NIST
Inp	301.38		NIST
Inp	301.69		NIST
Inp	301.75		NIST
Inp	301.26		NIST
Inp	301.08		NIST
Inp	301.69		NIST
Inp	301.50		NIST
Inp	318.50		NIST
Inp	319.50		NIST
Inp	301.53		NIST
Inp	301.38		NIST
Inp	301.53		NIST
Inp	301.20		NIST
Inp	301.40		NIST
Inp	303.03		NIST
Inp	301.37		NIST
Inp	301.39		NIST
Inp	301.20		NIST
Inp	301.40		NIST
Inp	301.50		NIST
Inp	301.70		NIST
Inp	301.40		NIST
Inp	301.39		NIST
Inp	301.39		NIST
Inp	301.69		NIST
Inp	301.38		NIST
Inp	301.70		NIST
Inp	301.69		NIST
Inp	301.08		NIST
Inp	301.05		NIST
Inp	301.17		NIST
Inp	301.69		NIST
Inp	301.73		NIST
Inp	301.92		NIST
Inp	301.92		NIST
Inp	301.40		NIST
Inp	301.69		NIST
Inp	301.29		NIST
Inp	301.52		NIST
Inp	301.69		NIST
Inp	301.87		NIST
Inp	1754.97		NIST
Inp	1759.00		NIST
Inp	301.50		NIST
Inp	301.53		NIST
Inp	301.39		NIST
Inp	301.40		NIST
Inp	301.70		NIST
Inp	301.69		NIST
Inp	301.68		NIST
Inp	301.41		NIST
Inp	301.67		NIST
Inp	301.35		NIST
Inp	301.76		NIST
Inp	301.38		NIST
Inp	1767.00		NIST
Inp	1770.90		NIST
Inp	1764.27		NIST
Inp	1782.28		NIST
Inp	1757.98		NIST
Inp	1749.00		NIST
Inp	1762.00		NIST
Inp	1770.00		NIST
Inp	1750.00		NIST
I	[300.41; 2746.00]
I	2728.00		NIST
I	2746.00		NIST
I	2740.00		NIST
I	2733.00		NIST
I	2740.00		NIST
I	Outlier 300.41		NIST
I	2740.00		NIST
S°solid,1 bar	[207.15; 207.50]	J/mol×K
S°solid,1 bar	207.15	J/mol×K	NIST
S°solid,1 bar	207.15	J/mol×K	NIST
S°solid,1 bar	207.50	J/mol×K	NIST
Tboil	[613.00; 615.00]	K
Tboil	615.00	K	KDB
Tboil	613.20	K	NIST
Tboil	613.00	K	NIST
Tboil	613.10 ± 0.30	K	NIST
Tboil	613.00 ± 5.00	K	NIST
Tc	[869.30; 894.00]	K
Tc	869.30	K	KDB
Tc	894.00	K	Critica...
Tfus	[488.00; 490.15]	K
Tfus	489.34	K	Aq. Sol...
Tfus	489.70	K	KDB
Tfus	490.05	K	Thermoc...
Tfus	489.70	K	Isother...
Tfus	490.15	K	Solubil...
Tfus	489.00	K	Solubil...
Tfus	488.00	K	Solubil...
Tfus	488.00	K	Solubil...
Ttriple	488.93 ± 0.01	K	NIST
Vc	0.554	m3/kmol	KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[334.16; 406.65]	J/mol×K	[589.34; 843.18]
Cp,gas	334.16	J/mol×K	589.34	Joback Calculated Property
Cp,gas	349.09	J/mol×K	631.65	Joback Calculated Property
Cp,gas	362.69	J/mol×K	673.95	Joback Calculated Property
Cp,gas	375.10	J/mol×K	716.26	Joback Calculated Property
Cp,gas	386.47	J/mol×K	758.56	Joback Calculated Property
Cp,gas	396.94	J/mol×K	800.87	Joback Calculated Property
Cp,gas	406.65	J/mol×K	843.18	Joback Calculated Property
Cp,solid	[207.10; 221.80]	J/mol×K	[297.20; 298.15]
Cp,solid	207.10	J/mol×K	297.20	NIST
Cp,solid	211.70	J/mol×K	298.15	NIST
Cp,solid	210.50	J/mol×K	298.15	NIST
Cp,solid	210.50	J/mol×K	298.15	NIST
Cp,solid	217.50	J/mol×K	298.15	NIST
Cp,solid	221.80	J/mol×K	298.15	NIST
η	[0.0004678; 0.0014969]	Pa×s	[351.88; 589.34]
η	0.0014969	Pa×s	351.88	Joback Calculated Property
η	0.0011180	Pa×s	391.46	Joback Calculated Property
η	0.0008810	Pa×s	431.03	Joback Calculated Property
η	0.0007226	Pa×s	470.61	Joback Calculated Property
η	0.0006112	Pa×s	510.19	Joback Calculated Property
η	0.0005296	Pa×s	549.76	Joback Calculated Property
η	0.0004678	Pa×s	589.34	Joback Calculated Property
ΔfusH	[28.80; 31.50]	kJ/mol	[483.00; 491.00]
ΔfusH	29.80	kJ/mol	483.00	NIST
ΔfusH	29.37	kJ/mol	488.90	NIST
ΔfusH	29.37	kJ/mol	488.90	NIST
ΔfusH	29.37	kJ/mol	488.93	NIST
ΔfusH	28.80	kJ/mol	489.40	NIST
ΔfusH	28.87	kJ/mol	489.70	NIST
ΔfusH	28.83	kJ/mol	490.00	NIST
ΔfusH	31.50	kJ/mol	491.00	NIST
ΔsubH	[84.10; 103.40]	kJ/mol	[303.00; 455.50]
ΔsubH	96.00 ± 6.00	kJ/mol	303.00	NIST
ΔsubH	91.80 ± 0.90	kJ/mol	303.00	NIST
ΔsubH	103.30 ± 2.90	kJ/mol	303.00	NIST
ΔsubH	84.10	kJ/mol	324.00	NIST
ΔsubH	98.40 ± 0.70	kJ/mol	335.00	NIST
ΔsubH	90.00 ± 1.30	kJ/mol	336.50	NIST
ΔsubH	95.60 ± 1.20	kJ/mol	337.00	NIST
ΔsubH	97.90 ± 0.60	kJ/mol	337.50	NIST
ΔsubH	103.40 ± 2.90	kJ/mol	338.00	NIST
ΔsubH	91.20	kJ/mol	338.00	NIST
ΔsubH	102.60	kJ/mol	338.00	NIST
ΔsubH	102.09	kJ/mol	338.70	NIST
ΔsubH	100.00 ± 2.80	kJ/mol	340.50	NIST
ΔsubH	98.49	kJ/mol	342.00	NIST
ΔsubH	98.70	kJ/mol	345.50	NIST
ΔsubH	102.10 ± 2.10	kJ/mol	345.50	NIST
ΔsubH	102.50	kJ/mol	345.50	NIST
ΔsubH	102.10	kJ/mol	346.00	NIST
ΔsubH	98.80 ± 0.40	kJ/mol	350.00	NIST
ΔsubH	97.20	kJ/mol	350.00	NIST
ΔsubH	98.30 ± 2.10	kJ/mol	350.50	NIST
ΔsubH	93.30 ± 0.80	kJ/mol	353.00	NIST
ΔsubH	93.30 ± 4.20	kJ/mol	353.00	NIST
ΔsubH	90.40	kJ/mol	353.00	NIST
ΔsubH	102.50 ± 1.90	kJ/mol	358.00	NIST
ΔsubH	92.00 ± 2.10	kJ/mol	364.00	NIST
ΔsubH	97.60 ± 1.30	kJ/mol	369.00	NIST
ΔsubH	94.80	kJ/mol	375.50	NIST
ΔsubH	94.30	kJ/mol	376.00	NIST
ΔsubH	99.70	kJ/mol	383.00	NIST
ΔsubH	97.30 ± 1.20	kJ/mol	388.00	NIST
ΔsubH	101.00 ± 0.50	kJ/mol	392.50	NIST
ΔsubH	99.70	kJ/mol	393.00	NIST
ΔsubH	97.00 ± 2.00	kJ/mol	396.00	NIST
ΔsubH	98.80 ± 0.40	kJ/mol	405.50	NIST
ΔsubH	98.00 ± 2.00	kJ/mol	408.50	NIST
ΔsubH	94.50	kJ/mol	455.50	NIST
ΔvapH	[58.60; 98.80]	kJ/mol	[298.00; 559.50]
ΔvapH	78.49	kJ/mol	298.00	Enthalp...
ΔvapH	98.80	kJ/mol	390.00	Evaluat...
ΔvapH	72.40	kJ/mol	398.00	NIST
ΔvapH	69.70	kJ/mol	398.00	NIST
ΔvapH	95.10	kJ/mol	453.15	Comment...
ΔvapH	66.70	kJ/mol	498.00	NIST
ΔvapH	62.10	kJ/mol	500.00	NIST
ΔvapH	59.60	kJ/mol	555.00	NIST
ΔvapH	60.70	kJ/mol	555.00	NIST
ΔvapH	59.20	kJ/mol	558.00	NIST
ΔvapH	60.30	kJ/mol	558.00	NIST
ΔvapH	58.60	kJ/mol	559.50	NIST
Psub	[1.79e-07; 5.93]	kPa	[284.15; 509.15]
Psub	1.79e-07	kPa	284.15	Determi...
Psub	3.52e-07	kPa	289.15	Determi...
Psub	6.77e-07	kPa	294.15	Determi...
Psub	1.27e-06	kPa	299.15	Determi...
Psub	2.35e-06	kPa	304.15	Determi...
Psub	2.79e-06	kPa	308.62	Measure...
Psub	4.25e-06	kPa	309.15	Determi...
Psub	5.41e-06	kPa	313.70	Measure...
Psub	7.54e-06	kPa	314.15	Determi...
Psub	1.31e-05	kPa	319.15	Determi...
Psub	1.30e-05	kPa	319.60	Sublima...
Psub	1.29e-05	kPa	319.60	Sublima...
Psub	1.76e-05	kPa	320.20	Vapor P...
Psub	1.91e-05	kPa	321.20	Vapor P...
Psub	1.80e-05	kPa	321.79	Develop...
Psub	1.70e-05	kPa	321.79	Develop...
Psub	1.70e-05	kPa	321.79	Develop...
Psub	1.80e-05	kPa	321.79	Develop...
Psub	1.90e-05	kPa	321.79	Develop...
Psub	1.80e-05	kPa	321.79	Develop...
Psub	1.60e-05	kPa	322.20	Vapor P...
Psub	2.47e-05	kPa	323.00	Vapor P...
Psub	1.83e-05	kPa	323.59	Measure...
Psub	2.14e-05	kPa	323.90	Sublima...
Psub	2.25e-05	kPa	324.15	Determi...
Psub	3.14e-05	kPa	326.10	Vapor P...
Psub	3.47e-05	kPa	326.60	Vapor P...
Psub	3.04e-05	kPa	326.80	Sublima...
Psub	3.00e-05	kPa	326.90	Sublima...
Psub	2.60e-05	kPa	327.00	Vapor P...
Psub	4.55e-05	kPa	328.20	Vapor P...
Psub	4.00e-05	kPa	328.88	Develop...
Psub	3.70e-05	kPa	328.88	Develop...
Psub	3.90e-05	kPa	328.88	Develop...
Psub	3.70e-05	kPa	328.88	Develop...
Psub	3.90e-05	kPa	328.88	Develop...
Psub	4.00e-05	kPa	328.88	Develop...
Psub	3.90e-05	kPa	328.88	Develop...
Psub	3.33e-05	kPa	329.10	Vapor P...
Psub	3.79e-05	kPa	329.15	Determi...
Psub	5.56e-05	kPa	330.80	Vapor P...
Psub	5.39e-05	kPa	331.50	Vapor P...
Psub	5.29e-05	kPa	331.70	Sublima...
Psub	6.52e-05	kPa	331.80	Vapor P...
Psub	5.32e-05	kPa	332.10	Sublima...
Psub	5.41e-05	kPa	332.20	Sublima...
Psub	7.73e-05	kPa	333.30	Vapor P...
Psub	4.91e-05	kPa	333.40	Vapor P...
Psub	5.99e-05	kPa	333.63	Measure...
Psub	6.51e-05	kPa	334.00	Sublima...
Psub	6.29e-05	kPa	334.15	Determi...
Psub	6.59e-05	kPa	334.20	Sublima...
Psub	7.28e-05	kPa	334.30	Vapor P...
Psub	8.46e-05	kPa	334.60	Vapor P...
Psub	1.07e-04	kPa	336.00	Vapor P...
Psub	7.20e-05	kPa	336.30	Vapor P...
Psub	9.16e-05	kPa	337.00	Sublima...
Psub	9.80e-05	kPa	337.20	Develop...
Psub	8.80e-05	kPa	337.20	Develop...
Psub	9.30e-05	kPa	337.20	Develop...
Psub	9.00e-05	kPa	337.20	Develop...
Psub	1.13e-04	kPa	337.20	Vapor P...
Psub	8.60e-05	kPa	337.20	Develop...
Psub	1.03e-04	kPa	337.20	Develop...
Psub	9.50e-05	kPa	337.20	Develop...
Psub	1.33e-04	kPa	338.50	Vapor P...
Psub	9.43e-05	kPa	338.70	Vapor P...
Psub	1.03e-04	kPa	339.15	Determi...
Psub	1.04e-04	kPa	339.25	Thermal...
Psub	1.13e-04	kPa	339.40	Sublima...
Psub	1.51e-04	kPa	340.10	Vapor P...
Psub	1.33e-04	kPa	340.10	Vapor P...
Psub	1.10e-04	kPa	340.40	Vapor P...
Psub	1.44e-04	kPa	340.41	The des...
Psub	1.43e-04	kPa	340.41	The des...
Psub	1.41e-04	kPa	340.41	The des...
Psub	1.19e-04	kPa	341.20	Vapor P...
Psub	1.70e-04	kPa	341.20	Vapor P...
Psub	1.49e-04	kPa	342.00	Sublima...
Psub	1.73e-04	kPa	342.25	The des...
Psub	1.67e-04	kPa	342.25	The des...
Psub	1.72e-04	kPa	342.25	The des...
Psub	1.31e-04	kPa	342.30	Vapor P...
Psub	1.96e-04	kPa	342.70	Vapor P...
Psub	1.77e-04	kPa	343.00	Vapor P...
Psub	1.92e-04	kPa	343.29	Reconci...
Psub	1.82e-04	kPa	343.30	Reconci...
Psub	1.97e-04	kPa	343.31	Reconci...
Psub	1.64e-04	kPa	343.60	Measure...
Psub	1.41e-04	kPa	343.60	Vapor P...
Psub	2.32e-04	kPa	343.70	Vapor P...
Psub	2.06e-04	kPa	344.06	The des...
Psub	2.11e-04	kPa	344.06	The des...
Psub	1.66e-04	kPa	344.15	Determi...
Psub	1.64e-04	kPa	344.20	Vapor P...
Psub	2.52e-04	kPa	345.50	Vapor P...
Psub	2.32e-04	kPa	345.60	Vapor P...
Psub	2.40e-04	kPa	345.76	Reconci...
Psub	2.35e-04	kPa	345.76	Reconci...
Psub	2.38e-04	kPa	345.77	Develop...
Psub	2.34e-04	kPa	345.77	Develop...
Psub	2.37e-04	kPa	345.77	Develop...
Psub	2.35e-04	kPa	345.77	Develop...
Psub	2.27e-04	kPa	345.77	Develop...
Psub	2.36e-04	kPa	345.77	Develop...
Psub	2.47e-04	kPa	345.79	Reconci...
Psub	1.92e-04	kPa	346.40	Vapor P...
Psub	2.63e-04	kPa	346.40	The des...
Psub	2.58e-04	kPa	346.40	The des...
Psub	2.62e-04	kPa	346.40	The des...
Psub	2.92e-04	kPa	346.40	Vapor P...
Psub	3.20e-04	kPa	347.80	Vapor P...
Psub	3.06e-04	kPa	348.15	The des...
Psub	3.08e-04	kPa	348.15	The des...
Psub	3.04e-04	kPa	348.15	The des...
Psub	2.60e-04	kPa	348.20	Vapor P...
Psub	3.05e-04	kPa	348.21	Reconci...
Psub	3.17e-04	kPa	348.21	Reconci...
Psub	2.97e-04	kPa	348.27	Reconci...
Psub	2.89e-04	kPa	348.35	Thermal...
Psub	3.13e-04	kPa	348.60	Vapor P...
Psub	2.63e-04	kPa	349.15	Determi...
Psub	3.16e-04	kPa	349.70	Sublima...
Psub	3.12e-04	kPa	349.70	Sublima...
Psub	3.76e-04	kPa	350.15	The des...
Psub	3.75e-04	kPa	350.15	The des...
Psub	3.71e-04	kPa	350.15	The des...
Psub	3.92e-04	kPa	350.75	Reconci...
Psub	4.01e-04	kPa	350.76	Reconci...
Psub	3.84e-04	kPa	350.79	Reconci...
Psub	4.15e-04	kPa	350.80	Vapor P...
Psub	3.98e-04	kPa	351.30	Vapor P...
Psub	4.11e-04	kPa	351.60	Vapor P...
Psub	4.58e-04	kPa	352.39	The des...
Psub	4.64e-04	kPa	352.39	The des...
Psub	4.59e-04	kPa	352.39	The des...
Psub	4.73e-04	kPa	352.86	Develop...
Psub	4.44e-04	kPa	352.86	Develop...
Psub	4.85e-04	kPa	352.86	Develop...
Psub	4.34e-04	kPa	352.86	Develop...
Psub	4.55e-04	kPa	352.86	Develop...
Psub	4.82e-04	kPa	352.86	Develop...
Psub	4.85e-04	kPa	353.04	Reconci...
Psub	4.79e-04	kPa	353.04	Reconci...
Psub	4.98e-04	kPa	353.19	Reconci...
Psub	5.54e-04	kPa	354.06	The des...
Psub	5.50e-04	kPa	354.06	The des...
Psub	5.48e-04	kPa	354.06	The des...
Psub	5.22e-04	kPa	354.10	Vapor P...
Psub	4.13e-04	kPa	354.15	Determi...
Psub	5.08e-04	kPa	354.80	Sublima...
Psub	6.30e-04	kPa	355.68	Reconci...
Psub	6.26e-04	kPa	355.73	Reconci...
Psub	6.23e-04	kPa	355.74	Reconci...
Psub	6.79e-04	kPa	356.20	The des...
Psub	6.58e-04	kPa	356.20	The des...
Psub	6.73e-04	kPa	356.20	The des...
Psub	7.99e-04	kPa	358.14	Reconci...
Psub	7.84e-04	kPa	358.15	Reconci...
Psub	7.98e-04	kPa	358.18	Reconci...
Psub	8.10e-04	kPa	358.22	The des...
Psub	8.21e-04	kPa	358.22	The des...
Psub	8.15e-04	kPa	358.22	The des...
Psub	6.40e-04	kPa	359.15	Determi...
Psub	9.80e-04	kPa	360.38	The des...
Psub	1.01e-03	kPa	360.38	The des...
Psub	9.78e-04	kPa	360.45	Thermal...
Psub	1.00e-03	kPa	360.63	Reconci...
Psub	9.92e-04	kPa	360.64	Develop...
Psub	9.88e-04	kPa	360.64	Develop...
Psub	9.93e-04	kPa	360.64	Develop...
Psub	9.80e-04	kPa	360.64	Develop...
Psub	9.42e-04	kPa	360.64	Develop...
Psub	9.92e-04	kPa	360.66	Reconci...
Psub	9.98e-04	kPa	360.68	Reconci...
Psub	1.23e-03	kPa	362.95	Reconci...
Psub	1.23e-03	kPa	362.95	Reconci...
Psub	1.24e-03	kPa	363.13	Reconci...
Psub	9.79e-04	kPa	364.15	Determi...
Psub	1.55e-03	kPa	365.54	Reconci...
Psub	1.55e-03	kPa	365.55	Reconci...
Psub	1.56e-03	kPa	365.56	Reconci...
Psub	1.58e-03	kPa	365.66	Thermal...
Psub	1.95e-03	kPa	367.97	Reconci...
Psub	1.93e-03	kPa	367.97	Reconci...
Psub	1.94e-03	kPa	367.98	Reconci...
Psub	1.48e-03	kPa	369.15	Determi...
Psub	1.18e-03	kPa	369.85	Thermal...
Psub	2.40e-03	kPa	370.43	Reconci...
Psub	2.42e-03	kPa	370.44	Reconci...
Psub	2.41e-03	kPa	370.44	Reconci...
Psub	2.98e-03	kPa	372.85	Reconci...
Psub	2.98e-03	kPa	372.89	Reconci...
Psub	2.97e-03	kPa	372.89	Reconci...
Psub	3.11e-03	kPa	373.95	Thermal...
Psub	2.22e-03	kPa	374.15	Determi...
Psub	3.58e-03	kPa	376.95	Thermal...
Psub	3.28e-03	kPa	379.15	Determi...
Psub	4.16e-03	kPa	379.55	Thermal...
Psub	5.77e-04	kPa	383.95	Thermal...
Psub	4.81e-03	kPa	384.15	Determi...
Psub	8.13e-03	kPa	386.45	Thermal...
Psub	9.62e-03	kPa	389.05	Thermal...
Psub	8.75e-03	kPa	389.05	Thermal...
Psub	6.98e-03	kPa	389.15	Determi...
Psub	0.01	kPa	392.95	Thermal...
Psub	0.01	kPa	393.75	Thermal...
Psub	0.01	kPa	393.75	Thermal...
Psub	0.01	kPa	394.15	Determi...
Psub	0.02	kPa	398.05	Thermal...
Psub	0.02	kPa	398.55	Thermal...
Psub	0.02	kPa	398.55	Thermal...
Psub	0.01	kPa	399.15	Determi...
Psub	0.02	kPa	404.15	Determi...
Psub	0.03	kPa	409.15	Determi...
Psub	0.04	kPa	414.15	Determi...
Psub	0.05	kPa	419.15	Determi...
Psub	0.07	kPa	424.15	Determi...
Psub	0.10	kPa	429.15	Determi...
Psub	0.14	kPa	434.15	Determi...
Psub	0.18	kPa	439.15	Determi...
Psub	0.24	kPa	444.15	Determi...
Psub	0.32	kPa	449.15	Determi...
Psub	0.42	kPa	454.15	Determi...
Psub	0.55	kPa	459.15	Determi...
Psub	0.71	kPa	464.15	Determi...
Psub	0.92	kPa	469.15	Determi...
Psub	1.18	kPa	474.15	Determi...
Psub	1.51	kPa	479.15	Determi...
Psub	1.92	kPa	484.15	Determi...
Psub	2.42	kPa	489.15	Determi...
Psub	3.05	kPa	494.15	Determi...
Psub	3.83	kPa	499.15	Determi...
Psub	4.77	kPa	504.15	Determi...
Psub	5.93	kPa	509.15	Determi...
Pvap	[5.79; 10.31]	kPa	[494.00; 512.00]
Pvap	5.79	kPa	494.00	Enthalp...
Pvap	6.24	kPa	496.00	Enthalp...
Pvap	6.71	kPa	498.00	Enthalp...
Pvap	7.17	kPa	500.00	Enthalp...
Pvap	7.66	kPa	502.00	Enthalp...
Pvap	8.17	kPa	504.00	Enthalp...
Pvap	8.69	kPa	506.00	Enthalp...
Pvap	9.23	kPa	508.00	Enthalp...
Pvap	9.77	kPa	510.00	Enthalp...
Pvap	10.31	kPa	512.00	Enthalp...
ΔfusS	[58.00; 60.07]	J/mol×K	[488.93; 490.00]
ΔfusS	60.07	J/mol×K	488.93	NIST
ΔfusS	59.00	J/mol×K	489.70	NIST
ΔfusS	58.00	J/mol×K	490.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[442.59; 710.04]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			7.28449e+00
Coefficient B			-7.34909e+02
Coefficient C			-3.37556e+02
Temperature range, min.			442.59
Temperature range, max.			710.04
Pvap	1.33	kPa	442.59	Calculated Property
Pvap	6.24	kPa	472.31	Calculated Property
Pvap	16.71	kPa	502.02	Calculated Property
Pvap	33.11	kPa	531.74	Calculated Property
Pvap	54.72	kPa	561.46	Calculated Property
Pvap	80.38	kPa	591.17	Calculated Property
Pvap	108.93	kPa	620.89	Calculated Property
Pvap	139.34	kPa	650.61	Calculated Property
Pvap	170.79	kPa	680.32	Calculated Property
Pvap	202.65	kPa	710.04	Calculated Property
Pvap	[1.52; 2781.06]	kPa	[453.15; 873.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.65652e+01
Coefficient B			-1.14763e+04
Coefficient C			-1.00600e+01
Coefficient D			3.45989e-06
Temperature range, min.			453.15
Temperature range, max.			873.00
Pvap	1.52	kPa	453.15	Calculated Property
Pvap	7.05	kPa	499.80	Calculated Property
Pvap	24.15	kPa	546.45	Calculated Property
Pvap	66.41	kPa	593.10	Calculated Property
Pvap	155.10	kPa	639.75	Calculated Property
Pvap	320.30	kPa	686.40	Calculated Property
Pvap	602.37	kPa	733.05	Calculated Property
Pvap	1054.77	kPa	779.70	Calculated Property
Pvap	1748.73	kPa	826.35	Calculated Property
Pvap	2781.06	kPa	873.00	Calculated Property

Similar Compounds

Find more compounds similar to Anthracene.

Mixtures

• Anthracene + 2-Pyrrolidinone, 1-methyl-
• Dibenzofuran + Anthracene
• Anthracene + Acenaphthene
• Anthracene + Fluorene
• 9-Bromoanthracene + Anthracene
• Phenanthrene + Anthracene
• Anthracene + Ethanol
• Acetonitrile + Anthracene
• n-Hexane + Anthracene
• Anthracene + Acetone
• Anthracene + Carbon Tetrachloride
• Anthracene + Benzene, chloro-
• Trichloromethane + Anthracene
• Carbon dioxide + Anthracene
• n-Hexane + Diisopropyl ether + Anthracene
• Diisopropyl ether + Anthracene + Heptane
• Diisopropyl ether + Anthracene + Octane
• Diisopropyl ether + Anthracene + Cyclohexane
• Diisopropyl ether + Anthracene + Cyclohexane, methyl-
• Diisopropyl ether + Anthracene + Pentane, 2,2,4-trimethyl-

Find more mixtures with Anthracene.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Enhancement of the anthracene aqueous solubility by a synergistic effect of alcohols and beta-cyclodextrin
• Solid-liquid phase equilibrium of 9-fluorenone and several polynuclear aromatic hydrocarbons
• Solid-liquid equilibrium of some polycyclic aromatic hydrocarbons in wash oil
• Thermochemical and vapor pressure behavior of anthracene and brominated anthracene mixtures
• Solubility of flavone, 6-methoxyflavone and anthracene in supercritical CO2 with/without a co-solvent of ethanol correlated by using a newly proposed entropy-based solubility parameter
• The design, construction, and testing of a new Knudsen effusion apparatus
• Calibration and test of an aneroid mini-bomb combustion calorimeter
• Temperature and sodium chloride effects on the solubility of anthracene in water
• New Knudsen effusion apparatus with simultaneous gravimetric and quartz crystal microbalance mass loss detection
• Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
• Critical point measurement of some polycyclic aromatic hydrocarbons
• Thermodynamic study of (anthracene + phenanthrene) solid state mixtures
• Reconciled thermophysical data for anthracene
• Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
• Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
• Evaluation of sublimation enthalpy by thermogravimetry: Analysis of the diffusion effects in the case of methyl and phenyl substituted hydantoins
• Comment on Studies on Thermodynamic Properties of FOX-7 and Its Five Closed-Loop Derivatives
• Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
• Measuring the Solubility of Anthracene and Chrysene in Supercritical Fluid Carbon Dioxide Using Static Solubility Apparatus Directly Interfaced Online to Supercritical Fluid Chromatography
• Isothermal Thermogravimetric Study for Determining Sublimation Enthalpies of Some Hydroxyflavones
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Solubility of Collinin and Isocollinin in Pressurized Carbon Dioxide: Synthesis, Solubility Parameters, and Equilibrium Measurements
• Solubility of Anthracene in Binary Alcohol + Acetonitrile Solvent Mixtures at 298.2 K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + 2-Methyl-1-butanol Mixtures at 298.2 K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Carbon Tetrachloride Mixtures at 298.2 K
• Thermodynamic Functions for Transfer of Anthracene from Water to (Water + Alcohol) Mixtures at 298.15K
• Solubility of Acenaphthene, Anthracene, and Pyrene in Water At 50 C to 300 C
• Vapor Pressure Characterization of Several Phenolics and Polyhydric Compounds by Knudsen Effusion Method
• Solubility of Solid Polycyclic Aromatic Hydrocarbons in Pressurized Hot Water at Temperatures from 313 K to the Melting Point
• Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
• Solubility of Anthracene in N,N-Dimethyformamide, N,N-Dimethylacetamide, and N-Methyl-2-pyrrolidone
• Solubility of Anthracene in C1-C3 Alcohols from (298.2 to 333.2) K and Their Mixtures with 2-Propanone at 298.2 K
• Solubility of Anthracene and Phenanthrene in Ethanol + 2,2,4-Trimethylpentane Mixtures at Different Temperatures
• Measurement and Modeling of the Solubility of Anthracene and Carbazole in Compressed Isobutane
• Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
• Measurement of Vapor Pressures of Selected PBDEs, Hexabromobenzene, and 1,2-Bis(2,4,6-tribromophenoxy)ethane at Elevated Temperatures
• Solubility of Anthracene in Binary Diisopropyl Ether + Alcohol Solvent Mixtures at 298.15 K
• Solubility of Anthracene in Binary Propyl Acetate + Alcohol Solvent Mixtures at 298.15 K
• Vapor Pressures and Enthalpies of Sublimation of Ten Polycyclic Aromatic Hydrocarbons Determined via the Knudsen Effusion Method
• Infinite Dilution Binary Diffusion Coefficients of Hydrotreating Compounds in Tetradecane in the Temperature Range from (310 to 475) K
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Sublimation Thermodynamic Parameters for Cholesterol, Ergosterol,
• Thermal Stability, Sublimation Pressures, and Diffusion Coefficients of Anthracene, Pyrene, and Some Metal beta-Diketonates
• Solubility of Anthracene in Sub- and Supercritical Propane
• Solubility of Anthracene in Binary and Ternary Mixtures of Cyclohexanone, Ethyl Acetate, and Methanol at 298.2 K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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.
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