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

InChI

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

InChI Key

YNPNZTXNASCQKK-UHFFFAOYSA-N

Formula

C14H10

SMILES

c1ccc2c(c1)ccc1ccccc12

Molecular Weight¹

178.23

CAS

85-01-8

Other Names

• Phenanthren
• Phenanthrin
• Phenantrin

• PAff : Proton affinity (kJ/mol).
• 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_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 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_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).
• Δ_subS : Entropy of sublimation at a given temperature (J/mol×K).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• 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	[820.10; 825.70]	kJ/mol
PAff	825.70	kJ/mol	NIST
PAff	820.10	kJ/mol	NIST
BasG	[793.70; 795.00]	kJ/mol
BasG	795.00	kJ/mol	NIST
BasG	793.70	kJ/mol	NIST
μ	0.00	debye	KDB
EA	[-0.01; 0.31]	eV
EA	-0.01 ± 0.04	eV	NIST
EA	0.27 ± 0.04	eV	NIST
EA	0.31 ± 0.01	eV	NIST
EA	0.20	eV	NIST
ΔfG°	383.08	kJ/mol	Joback Calculated Property
ΔfH°gas	[163.60; 206.90]	kJ/mol
ΔfH°gas	202.20 ± 2.30	kJ/mol	NIST
ΔfH°gas	201.20 ± 4.70	kJ/mol	NIST
ΔfH°gas	206.90 ± 4.60	kJ/mol	NIST
ΔfH°gas	203.80	kJ/mol	NIST
ΔfH°gas	163.60	kJ/mol	NIST
ΔfH°solid	[72.80; 116.10]	kJ/mol
ΔfH°solid	110.10 ± 2.20	kJ/mol	NIST
ΔfH°solid	109.80 ± 1.60	kJ/mol	NIST
ΔfH°solid	116.10 ± 1.40	kJ/mol	NIST
ΔfH°solid	113.00	kJ/mol	NIST
ΔfH°solid	72.80 ± 2.60	kJ/mol	NIST
ΔfusH°	15.15	kJ/mol	Thermod...
ΔvapH°	[78.50; 79.00]	kJ/mol
ΔvapH°	78.70	kJ/mol	NIST
ΔvapH°	79.00 ± 1.20	kJ/mol	NIST
ΔvapH°	78.70	kJ/mol	NIST
ΔvapH°	78.50	kJ/mol	NIST
IE	[7.60; 23.10]	eV
IE	7.89 ± 0.00	eV	NIST
IE	7.90	eV	NIST
IE	7.87 ± 0.02	eV	NIST
IE	7.89 ± 0.00	eV	NIST
IE	7.89 ± 0.05	eV	NIST
IE	7.86	eV	NIST
IE	7.92 ± 0.05	eV	NIST
IE	7.86 ± 0.01	eV	NIST
IE	7.92	eV	NIST
IE	7.91 ± 0.01	eV	NIST
IE	8.08	eV	NIST
IE	7.69	eV	NIST
IE	7.75	eV	NIST
IE	8.03 ± 0.01	eV	NIST
IE	8.10 ± 0.04	eV	NIST
IE	8.03 ± 0.01	eV	NIST
IE	8.07	eV	NIST
IE	7.60	eV	NIST
IE	8.22	eV	NIST
IE	8.25	eV	NIST
IE	8.09	eV	NIST
IE	8.03	eV	NIST
IE	Outlier 23.10	eV	NIST
IE	8.03	eV	NIST
IE	8.02	eV	NIST
IE	7.91	eV	NIST
IE	7.85	eV	NIST
IE	7.86 ± 0.02	eV	NIST
IE	7.86	eV	NIST
IE	7.87 ± 0.02	eV	NIST
IE	7.92 ± 0.02	eV	NIST
log10WS	[-5.26; -5.26]
log10WS	-5.26		Aq. Sol...
log10WS	-5.26		Estimat...
logPoct/wat	3.993		Crippen Calculated Property
McVol	145.440	ml/mol	McGowan Calculated Property
Pc	3243.03	kPa	Joback Calculated Property
Inp	[1724.00; 1797.00]
Inp	1730.00		NIST
Inp	1745.00		NIST
Inp	1765.00		NIST
Inp	1761.00		NIST
Inp	Outlier 1724.00		NIST
Inp	1778.60		NIST
Inp	1775.00		NIST
Inp	1759.60		NIST
Inp	1778.40		NIST
Inp	1790.10		NIST
Inp	1776.30		NIST
Inp	1776.30		NIST
Inp	1756.90		NIST
Inp	1776.30		NIST
Inp	1789.20		NIST
Inp	1769.70		NIST
Inp	1791.20		NIST
Inp	1797.00		NIST
Inp	1759.30		NIST
Inp	1756.90		NIST
Inp	1776.30		NIST
Inp	1789.20		NIST
Inp	1776.30		NIST
Inp	1776.30		NIST
Inp	1794.00		NIST
Inp	1791.00		NIST
Inp	1776.00		NIST
Inp	1742.00		NIST
Inp	1730.00		NIST
Inp	1739.00		NIST
Inp	1739.00		NIST
Inp	1739.00		NIST
Inp	1739.00		NIST
Inp	1740.00		NIST
Inp	1753.00		NIST
Inp	1753.00		NIST
Inp	1753.00		NIST
Inp	1753.00		NIST
Inp	1754.00		NIST
Inp	1756.00		NIST
Inp	1757.00		NIST
Inp	1761.00		NIST
Inp	1763.00		NIST
Inp	1768.00		NIST
Inp	1744.70		NIST
Inp	1734.95		NIST
Inp	1741.00		NIST
Inp	1744.37		NIST
Inp	1784.21		NIST
Inp	Outlier 1724.00		NIST
Inp	1761.00		NIST
Inp	1749.00		NIST
Inp	1729.00		NIST
Inp	1792.00		NIST
Inp	1775.00		NIST
Inp	1775.00		NIST
Inp	1749.00		NIST
Inp	1784.00		NIST
Inp	1784.00		NIST
Inp	1775.00		NIST
Inp	1784.00		NIST
Inp	1752.00		NIST
Inp	1760.00		NIST
Inp	1784.70		NIST
Inp	1776.00		NIST
Inp	1777.00		NIST
Inp	1779.00		NIST
Inp	1780.00		NIST
Inp	1781.00		NIST
Inp	1782.00		NIST
Inp	1792.00		NIST
Inp	1793.00		NIST
Inp	1769.00		NIST
Inp	1751.00		NIST
Inp	1744.00		NIST
Inp	1744.00		NIST
Inp	1767.00		NIST
Inp	1772.00		NIST
Inp	1741.00		NIST
Inp	1752.00		NIST
Inp	1784.00		NIST
Inp	1780.00		NIST
Inp	1768.00		NIST
Inp	1770.00		NIST
Inp	1755.00		NIST
Inp	1794.00		NIST
Inp	1797.00		NIST
Inp	1747.00		NIST
Inp	1786.00		NIST
Inp	1786.00		NIST
Inp	1741.00		NIST
Inp	1770.00		NIST
Inp	1786.00		NIST
I	[2712.00; 2723.00]
I	2722.00		NIST
I	2723.00		NIST
I	2712.00		NIST
I	2722.00		NIST
S°solid,1 bar	[211.70; 215.06]	J/mol×K
S°solid,1 bar	215.06	J/mol×K	NIST
S°solid,1 bar	211.70	J/mol×K	NIST
Tboil	[601.15; 613.20]	K
Tboil	613.00	K	KDB
Tboil	609.20	K	NIST
Tboil	613.20	K	NIST
Tboil	605.15 ± 5.00	K	NIST
Tboil	601.15 ± 3.00	K	NIST
Tboil	613.15 ± 2.00	K	NIST
Tc	[869.00; 893.00]	K
Tc	869.00	K	KDB
Tc	893.00	K	Critica...
Tc	869.00 ± 1.00	K	NIST
Tc	869.30 ± 1.00	K	NIST
Tfus	[369.40; 645.70]	K
Tfus	372.71	K	Aq. Sol...
Tfus	372.39	K	KDB
Tfus	378.07	K	Solubil...
Tfus	Outlier 645.70 ± 0.40	K	NIST
Tfus	372.74 ± 0.20	K	NIST
Tfus	370.00 ± 1.50	K	NIST
Tfus	372.00 ± 1.50	K	NIST
Tfus	373.00 ± 2.00	K	NIST
Tfus	373.15 ± 1.00	K	NIST
Tfus	372.80 ± 0.30	K	NIST
Tfus	371.30 ± 1.00	K	NIST
Tfus	373.15 ± 0.30	K	NIST
Tfus	371.80 ± 2.00	K	NIST
Tfus	371.20 ± 1.50	K	NIST
Tfus	371.90 ± 0.70	K	NIST
Tfus	372.70 ± 1.00	K	NIST
Tfus	373.00 ± 2.50	K	NIST
Tfus	372.05 ± 1.00	K	NIST
Tfus	374.00 ± 1.50	K	NIST
Tfus	372.11 ± 0.50	K	NIST
Tfus	372.32 ± 0.20	K	NIST
Tfus	372.60 ± 0.30	K	NIST
Tfus	372.77 ± 0.20	K	NIST
Tfus	372.30 ± 0.10	K	NIST
Tfus	372.90 ± 0.50	K	NIST
Tfus	373.00 ± 1.50	K	NIST
Tfus	371.40 ± 0.20	K	NIST
Tfus	374.20 ± 1.00	K	NIST
Tfus	373.00 ± 0.50	K	NIST
Tfus	371.70 ± 0.10	K	NIST
Tfus	371.40 ± 1.50	K	NIST
Tfus	369.50 ± 1.00	K	NIST
Tfus	371.15 ± 0.50	K	NIST
Tfus	374.15 ± 3.00	K	NIST
Tfus	378.65 ± 2.00	K	NIST
Tfus	372.95 ± 0.30	K	NIST
Tfus	418.00 ± 8.36	K	NIST
Tfus	369.40 ± 0.50	K	NIST
Ttriple	[339.52; 372.38]	K
Ttriple	339.52	K	Ternary...
Ttriple	372.38 ± 0.02	K	NIST
Ttriple	372.38 ± 0.02	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	[134.70; 267.40]	J/mol×K	[297.50; 343.00]
Cp,solid	233.50	J/mol×K	297.50	NIST
Cp,solid	207.10	J/mol×K	298.10	NIST
Cp,solid	226.40	J/mol×K	298.10	NIST
Cp,solid	220.62	J/mol×K	298.15	NIST
Cp,solid	134.70	J/mol×K	298.15	NIST
Cp,solid	220.30	J/mol×K	298.15	NIST
Cp,solid	267.40	J/mol×K	343.00	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	[15.72; 18.63]	kJ/mol	[368.00; 373.81]
ΔfusH	16.60	kJ/mol	368.00	NIST
ΔfusH	17.15	kJ/mol	371.40	NIST
ΔfusH	17.14	kJ/mol	371.70	NIST
ΔfusH	16.46	kJ/mol	372.40	NIST
ΔfusH	16.20	kJ/mol	372.90	NIST
ΔfusH	18.63	kJ/mol	373.00	NIST
ΔfusH	18.00	kJ/mol	373.20	NIST
ΔfusH	15.72	kJ/mol	373.81	NIST
ΔsubH	[81.60; 96.20]	kJ/mol	[213.00; 383.00]
ΔsubH	95.80 ± 2.90	kJ/mol	213.00	NIST
ΔsubH	84.10	kJ/mol	293.00	NIST
ΔsubH	84.10 ± 2.50	kJ/mol	297.00	NIST
ΔsubH	90.90	kJ/mol	298.15	NIST
ΔsubH	95.90	kJ/mol	303.00	NIST
ΔsubH	95.00 ± 0.60	kJ/mol	303.00	NIST
ΔsubH	86.61	kJ/mol	309.70	NIST
ΔsubH	84.10 ± 0.80	kJ/mol	313.00	NIST
ΔsubH	90.70 ± 1.20	kJ/mol	315.00	NIST
ΔsubH	86.60	kJ/mol	316.50	NIST
ΔsubH	95.00 ± 4.40	kJ/mol	318.00	NIST
ΔsubH	81.60	kJ/mol	323.00	NIST
ΔsubH	91.60 ± 0.40	kJ/mol	323.00	NIST
ΔsubH	84.10 ± 0.80	kJ/mol	323.00	NIST
ΔsubH	96.20	kJ/mol	335.50	NIST
ΔsubH	82.00 ± 2.00	kJ/mol	339.50	NIST
ΔsubH	87.20	kJ/mol	344.50	NIST
ΔsubH	87.20 ± 1.10	kJ/mol	350.00	NIST
ΔsubH	87.20	kJ/mol	372.00	NIST
ΔsubH	88.90	kJ/mol	383.00	NIST
ΔvapH	[57.20; 87.24]	kJ/mol	[298.00; 559.50]
ΔvapH	78.65	kJ/mol	298.00	Enthalp...
ΔvapH	87.24	kJ/mol	350.00	NIST
ΔvapH	71.20	kJ/mol	372.00	NIST
ΔvapH	71.20	kJ/mol	386.00	Evaluat...
ΔvapH	69.70	kJ/mol	390.00	NIST
ΔvapH	71.20	kJ/mol	398.00	NIST
ΔvapH	69.60	kJ/mol	398.00	NIST
ΔvapH	72.20	kJ/mol	398.00	NIST
ΔvapH	67.50	kJ/mol	420.00	NIST
ΔvapH	58.20	kJ/mol	502.00	NIST
ΔvapH	57.20	kJ/mol	548.00	NIST
ΔvapH	61.20	kJ/mol	548.00	NIST
ΔvapH	59.30	kJ/mol	559.50	NIST
ΔvapH	61.20	kJ/mol	559.50	NIST
Psub	[1.40e-05; 1.01e-03]	kPa	[295.73; 333.16]
Psub	1.50e-05	kPa	295.73	Develop...
Psub	1.40e-05	kPa	295.73	Develop...
Psub	1.40e-05	kPa	295.73	Develop...
Psub	1.40e-05	kPa	295.73	Develop...
Psub	1.40e-05	kPa	295.73	Develop...
Psub	1.50e-05	kPa	295.73	Develop...
Psub	1.50e-05	kPa	295.73	Develop...
Psub	3.20e-05	kPa	302.13	Develop...
Psub	3.20e-05	kPa	302.13	Develop...
Psub	3.10e-05	kPa	302.13	Develop...
Psub	3.10e-05	kPa	302.13	Develop...
Psub	3.20e-05	kPa	302.13	Develop...
Psub	3.20e-05	kPa	302.13	Develop...
Psub	3.20e-05	kPa	302.13	Develop...
Psub	6.20e-05	kPa	307.66	Develop...
Psub	6.10e-05	kPa	307.66	Develop...
Psub	6.40e-05	kPa	307.66	Develop...
Psub	6.10e-05	kPa	307.66	Develop...
Psub	6.10e-05	kPa	307.66	Develop...
Psub	6.10e-05	kPa	307.66	Develop...
Psub	1.19e-04	kPa	313.10	Develop...
Psub	1.19e-04	kPa	313.10	Develop...
Psub	1.19e-04	kPa	313.10	Develop...
Psub	1.18e-04	kPa	313.10	Develop...
Psub	1.18e-04	kPa	313.10	Develop...
Psub	1.23e-04	kPa	313.46	The des...
Psub	1.24e-04	kPa	313.46	The des...
Psub	1.24e-04	kPa	313.46	The des...
Psub	1.51e-04	kPa	315.48	The des...
Psub	1.55e-04	kPa	315.48	The des...
Psub	1.56e-04	kPa	315.48	The des...
Psub	1.85e-04	kPa	317.41	The des...
Psub	1.91e-04	kPa	317.41	The des...
Psub	1.93e-04	kPa	317.41	The des...
Psub	2.03e-04	kPa	318.47	Develop...
Psub	2.11e-04	kPa	318.47	Develop...
Psub	2.08e-04	kPa	318.47	Develop...
Psub	2.12e-04	kPa	318.47	Develop...
Psub	2.08e-04	kPa	318.47	Develop...
Psub	2.05e-04	kPa	318.47	Develop...
Psub	2.00e-04	kPa	318.47	Develop...
Psub	2.39e-04	kPa	319.47	The des...
Psub	2.35e-04	kPa	319.47	The des...
Psub	2.38e-04	kPa	319.47	The des...
Psub	2.96e-04	kPa	321.48	The des...
Psub	2.93e-04	kPa	321.48	The des...
Psub	2.92e-04	kPa	321.48	The des...
Psub	3.46e-04	kPa	323.00	Develop...
Psub	3.38e-04	kPa	323.00	Develop...
Psub	3.40e-04	kPa	323.00	Develop...
Psub	3.43e-04	kPa	323.00	Develop...
Psub	3.43e-04	kPa	323.00	Develop...
Psub	3.41e-04	kPa	323.00	Develop...
Psub	3.46e-04	kPa	323.00	Develop...
Psub	3.43e-04	kPa	323.16	The des...
Psub	3.52e-04	kPa	323.16	The des...
Psub	3.52e-04	kPa	323.16	The des...
Psub	4.53e-04	kPa	325.46	The des...
Psub	4.36e-04	kPa	325.46	The des...
Psub	4.46e-04	kPa	325.46	The des...
Psub	5.44e-04	kPa	327.47	The des...
Psub	5.50e-04	kPa	327.47	The des...
Psub	5.43e-04	kPa	327.47	The des...
Psub	5.79e-04	kPa	328.20	Develop...
Psub	5.90e-04	kPa	328.20	Develop...
Psub	5.99e-04	kPa	328.20	Develop...
Psub	5.83e-04	kPa	328.20	Develop...
Psub	5.94e-04	kPa	328.20	Develop...
Psub	5.74e-04	kPa	328.20	Develop...
Psub	6.70e-04	kPa	329.47	The des...
Psub	6.75e-04	kPa	329.47	The des...
Psub	6.78e-04	kPa	329.47	The des...
Psub	8.25e-04	kPa	331.42	The des...
Psub	8.34e-04	kPa	331.42	The des...
Psub	8.14e-04	kPa	331.42	The des...
Psub	9.58e-04	kPa	332.95	Develop...
Psub	9.38e-04	kPa	332.95	Develop...
Psub	9.64e-04	kPa	332.95	Develop...
Psub	9.42e-04	kPa	332.95	Develop...
Psub	9.59e-04	kPa	332.95	Develop...
Psub	9.60e-04	kPa	332.95	Develop...
Psub	1.01e-03	kPa	333.16	The des...
Psub	1.00e-03	kPa	333.16	The des...
Pvap	[0.06; 3.87]	kPa	[384.00; 480.00]
Pvap	0.06	kPa	384.00	Enthalp...
Pvap	0.08	kPa	388.00	Enthalp...
Pvap	0.10	kPa	392.00	Enthalp...
Pvap	0.11	kPa	396.00	Enthalp...
Pvap	0.15	kPa	400.00	Gas pha...
Pvap	0.15	kPa	400.00	Gas pha...
Pvap	0.14	kPa	400.00	Gas pha...
Pvap	0.15	kPa	400.00	Enthalp...
Pvap	0.16	kPa	400.00	Gas pha...
Pvap	0.18	kPa	404.00	Enthalp...
Pvap	0.19	kPa	405.00	Gas pha...
Pvap	0.18	kPa	405.00	Gas pha...
Pvap	0.18	kPa	405.00	Gas pha...
Pvap	0.18	kPa	405.00	Gas pha...
Pvap	0.21	kPa	408.00	Enthalp...
Pvap	0.22	kPa	410.00	Gas pha...
Pvap	0.22	kPa	410.00	Gas pha...
Pvap	0.22	kPa	410.00	Gas pha...
Pvap	0.23	kPa	410.00	Gas pha...
Pvap	0.24	kPa	412.00	Enthalp...
Pvap	0.28	kPa	415.00	Gas pha...
Pvap	0.28	kPa	415.00	Gas pha...
Pvap	0.28	kPa	415.00	Gas pha...
Pvap	0.27	kPa	415.00	Gas pha...
Pvap	0.29	kPa	416.00	Enthalp...
Pvap	0.34	kPa	420.00	Gas pha...
Pvap	0.34	kPa	420.00	Gas pha...
Pvap	0.34	kPa	420.00	Gas pha...
Pvap	0.35	kPa	420.00	Gas pha...
Pvap	0.35	kPa	420.00	Enthalp...
Pvap	0.43	kPa	425.00	Gas pha...
Pvap	0.42	kPa	425.00	Gas pha...
Pvap	0.43	kPa	425.00	Gas pha...
Pvap	0.43	kPa	425.00	Gas pha...
Pvap	0.52	kPa	430.00	Gas pha...
Pvap	0.53	kPa	430.00	Gas pha...
Pvap	0.53	kPa	430.00	Gas pha...
Pvap	0.54	kPa	430.00	Gas pha...
Pvap	0.64	kPa	435.00	Gas pha...
Pvap	0.67	kPa	435.00	Gas pha...
Pvap	0.66	kPa	435.00	Gas pha...
Pvap	0.65	kPa	435.00	Gas pha...
Pvap	0.80	kPa	440.00	Gas pha...
Pvap	0.81	kPa	440.00	Gas pha...
Pvap	0.80	kPa	440.00	Gas pha...
Pvap	0.82	kPa	440.00	Gas pha...
Pvap	0.98	kPa	445.00	Gas pha...
Pvap	1.00	kPa	445.00	Gas pha...
Pvap	0.99	kPa	445.00	Gas pha...
Pvap	1.01	kPa	445.00	Gas pha...
Pvap	1.20	kPa	450.00	Gas pha...
Pvap	1.22	kPa	450.00	Gas pha...
Pvap	1.24	kPa	450.00	Gas pha...
Pvap	1.24	kPa	450.00	Gas pha...
Pvap	1.50	kPa	455.00	Gas pha...
Pvap	1.47	kPa	455.00	Gas pha...
Pvap	1.52	kPa	455.00	Gas pha...
Pvap	1.52	kPa	455.00	Gas pha...
Pvap	1.82	kPa	460.00	Gas pha...
Pvap	1.85	kPa	460.00	Gas pha...
Pvap	1.79	kPa	460.00	Gas pha...
Pvap	1.84	kPa	460.00	Gas pha...
Pvap	2.17	kPa	465.00	Gas pha...
Pvap	2.23	kPa	465.00	Gas pha...
Pvap	2.21	kPa	465.00	Gas pha...
Pvap	2.24	kPa	465.00	Gas pha...
Pvap	2.62	kPa	470.00	Gas pha...
Pvap	2.66	kPa	470.00	Gas pha...
Pvap	2.70	kPa	470.00	Gas pha...
Pvap	2.70	kPa	470.00	Gas pha...
Pvap	3.20	kPa	475.00	Gas pha...
Pvap	3.25	kPa	475.00	Gas pha...
Pvap	3.25	kPa	475.00	Gas pha...
Pvap	3.15	kPa	475.00	Gas pha...
Pvap	3.87	kPa	480.00	Gas pha...
Pvap	3.82	kPa	480.00	Gas pha...
Pvap	3.87	kPa	480.00	Gas pha...
Pvap	3.77	kPa	480.00	Gas pha...
ΔfusS	[46.10; 49.90]	J/mol×K	[371.40; 373.20]
ΔfusS	46.20	J/mol×K	371.40	NIST
ΔfusS	46.10	J/mol×K	371.70	NIST
ΔfusS	49.90	J/mol×K	373.00	NIST
ΔfusS	48.20	J/mol×K	373.20	NIST
ΔsubS	304.90	J/mol×K	298.15	NIST
ΔvapS	249.30	J/mol×K	350.00	NIST

Pressure Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[451.00; 647.66]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.49964e+01
Coefficient B			-5.57632e+03
Coefficient C			-7.18810e+01
Temperature range, min.			451.00
Temperature range, max.			647.66
Pvap	1.33	kPa	451.00	Calculated Property
Pvap	2.97	kPa	472.85	Calculated Property
Pvap	6.10	kPa	494.70	Calculated Property
Pvap	11.66	kPa	516.55	Calculated Property
Pvap	20.98	kPa	538.40	Calculated Property
Pvap	35.81	kPa	560.26	Calculated Property
Pvap	58.40	kPa	582.11	Calculated Property
Pvap	91.48	kPa	603.96	Calculated Property
Pvap	138.31	kPa	625.81	Calculated Property
Pvap	202.66	kPa	647.66	Calculated Property
Pvap	[0.03; 2879.35]	kPa	[372.15; 869.25]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.07381e+02
Coefficient B			-1.29131e+04
Coefficient C			-1.29796e+01
Coefficient D			4.34300e-06
Temperature range, min.			372.15
Temperature range, max.			869.25
Pvap	0.03	kPa	372.15	Calculated Property
Pvap	0.51	kPa	427.38	Calculated Property
Pvap	4.19	kPa	482.62	Calculated Property
Pvap	20.44	kPa	537.85	Calculated Property
Pvap	70.53	kPa	593.08	Calculated Property
Pvap	191.15	kPa	648.32	Calculated Property
Pvap	436.94	kPa	703.55	Calculated Property
Pvap	885.07	kPa	758.78	Calculated Property
Pvap	1645.28	kPa	814.02	Calculated Property
Pvap	2879.35	kPa	869.25	Calculated Property

Similar Compounds

Find more compounds similar to Phenanthrene.

Mixtures

• Phenanthrene + Anthracene
• Phenanthrene + Formamide, N,N-dimethyl- + Carbazole
• Phenanthrene + Acetone + Carbazole
• Phenanthrene + Acetonitrile + Carbazole
• Phenanthrene + Toluene + Carbazole
• Phenanthrene + Formamide, N,N-dimethyl-
• Phenanthrene + Acetone
• Phenanthrene + Acetonitrile
• Phenanthrene + Toluene
• Phenanthrene + Carbazole
• Phenanthrene + Ethanol + Methyl Alcohol
• Phenanthrene + Isopropyl Alcohol + Methyl Alcohol
• Phenanthrene + Isopropyl Alcohol + Ethanol
• Phenanthrene + 1-Propanol + Isopropyl Alcohol
• Phenanthrene + Isopropyl Alcohol + 1-Butanol
• Phenanthrene + Methyl Alcohol
• Phenanthrene + 1-Propanol
• Phenanthrene + 1-Butanol
• Phenanthrene + Ethanol
• Phenanthrene + 1-Propanol + Methyl Alcohol

Find more mixtures with Phenanthrene.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Solubility of iodopropynyl butylcarbamate in supercritical carbon dioxide
• The design, construction, and testing of a new Knudsen effusion apparatus
• Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
• Gas phase enthalpies of formation of nitrobenzamides using combustion calorimetry and thermal analysis
• Critical point measurement of some polycyclic aromatic hydrocarbons
• Thermodynamic study of (anthracene + phenanthrene) solid state mixtures
• Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
• Combined experiments to measure low sublimation pressures and diffusion coefficients of organometallic compounds
• Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
• Evaluation of sublimation enthalpy by thermogravimetry: Analysis of the diffusion effects in the case of methyl and phenyl substituted hydantoins
• Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
• Phase Behavior Data of (CO2 + Toluene + Phenanthrene) and (CO2 + (Methanol + Phenanthrene) Systems at High Pressure
• Solubilities of Palmitic Acid + Capsaicin in Supercritical Carbon Dioxide
• Measurement of the Phase Behavior of the Ternary System Carbon Dioxide + Acetone + Phenanthrene
• Solubility of Anthracene and Phenanthrene in Ethanol + 2,2,4-Trimethylpentane Mixtures at Different Temperatures
• Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols + 2-Propanol and Ethanol + Methanol at 298.15 K
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols at 298.2 K
• 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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