Chemical Properties of Phenol, 2-methyl- (CAS 95-48-7)

InChI

InChI=1S/C7H8O/c1-6-4-2-3-5-7(6)8/h2-5,8H,1H3

InChI Key

QWVGKYWNOKOFNN-UHFFFAOYSA-N

Formula

C7H8O

SMILES

Cc1ccccc1O

Molecular Weight¹

108.14

CAS

95-48-7

Other Names

• 1-Methyl-2-hydroxybenzene
• 1-hydroxy-2-methylbenzene
• 2-Hydroxytoluene
• 2-cresol
• 2-methylphenol
• NSC 23076
• Orthocresol
• Rcra waste number U052
• o-Cresylic acid
• o-Kresol
• o-Methylphenylol
• o-Oxytoluene
• o-Toluol
• o-cresol
• o-hydroxytoluene
• o-methylphenol
• ortho-cresol
• ortho-hydroxytoluene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : 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_boil : Boiling point at given 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).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4330		KDB
PAff	832.00 ± 8.00	kJ/mol	NIST
BasG	800.00 ± 8.00	kJ/mol	NIST
ΔcH°liquid	-3696.00	kJ/mol	NIST
ΔcH°solid	[-3697.00; -3693.30]	kJ/mol
ΔcH°solid	-3693.60 ± 0.42	kJ/mol	NIST
ΔcH°solid	-3693.30 ± 1.00	kJ/mol	NIST
ΔcH°solid	-3697.00	kJ/mol	NIST
μ	1.60	debye	KDB
ΔfG°	-33.00	kJ/mol	KDB
ΔfH°gas	[-128.70; -128.30]	kJ/mol
ΔfH°gas	-128.70	kJ/mol	KDB
ΔfH°gas	-128.30 ± 0.88	kJ/mol	NIST
ΔfH°gas	-128.60 ± 0.92	kJ/mol	NIST
ΔfH°liquid	-202.00	kJ/mol	NIST
ΔfH°solid	[-204.60; -204.30]	kJ/mol
ΔfH°solid	-204.30	kJ/mol	NIST
ΔfH°solid	-204.60 ± 0.92	kJ/mol	NIST
ΔfusH°	13.71	kJ/mol	Joback Calculated Property
ΔsubH°	[73.70; 76.02]	kJ/mol
ΔsubH°	73.70 ± 0.50	kJ/mol	NIST
ΔsubH°	76.00	kJ/mol	NIST
ΔsubH°	76.02 ± 0.75	kJ/mol	NIST
ΔsubH°	76.00	kJ/mol	NIST
ΔvapH°	44.89	kJ/mol	NIST
IE	[8.14; 8.93]	eV
IE	8.14	eV	NIST
IE	8.24 ± 0.02	eV	NIST
IE	8.93	eV	NIST
IE	8.46 ± 0.06	eV	NIST
IE	8.50	eV	NIST
IE	8.48	eV	NIST
log10WS	[-0.62; -0.62]
log10WS	-0.62		Aq. Solubility Prediction
log10WS	-0.62		Estimated Solubility
logPoct/wat	1.701		Crippen Calculated Property
McVol	91.600	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	2		KDB
Pc	[4170.00; 5010.00]	kPa
Pc	5010.00	kPa	KDB
Pc	4170.00 ± 39.22	kPa	NIST
Pc	4863.60 ± 303.98	kPa	NIST
Pc	5005.46 ± 70.92	kPa	NIST
Inp	[170.20; 1080.00]
Inp	1030.00		NIST
Inp	1027.00		NIST
Inp	1032.00		NIST
Inp	1014.30		NIST
Inp	1017.60		NIST
Inp	1007.00		NIST
Inp	1008.00		NIST
Inp	1029.00		NIST
Inp	1030.00		NIST
Inp	1030.00		NIST
Inp	1040.00		NIST
Inp	1048.00		NIST
Inp	1078.00		NIST
Inp	1039.00		NIST
Inp	1035.00		NIST
Inp	1052.00		NIST
Inp	1042.70		NIST
Inp	1071.00		NIST
Inp	1073.00		NIST
Inp	1031.10		NIST
Inp	1054.00		NIST
Inp	1080.00		NIST
Inp	1042.00		NIST
Inp	1029.70		NIST
Inp	1032.00		NIST
Inp	1042.00		NIST
Inp	1044.00		NIST
Inp	1029.00		NIST
Inp	1055.00		NIST
Inp	1068.00		NIST
Inp	1068.00		NIST
Inp	1051.80		NIST
Inp	1052.90		NIST
Inp	1052.00		NIST
Inp	1030.00		NIST
Inp	1034.00		NIST
Inp	1034.00		NIST
Inp	1054.00		NIST
Inp	1077.00		NIST
Inp	1072.00		NIST
Inp	1053.00		NIST
Inp	1054.00		NIST
Inp	1058.00		NIST
Inp	1060.00		NIST
Inp	1054.00		NIST
Inp	1030.00		NIST
Inp	1033.00		NIST
Inp	1052.00		NIST
Inp	1053.00		NIST
Inp	1027.00		NIST
Inp	1038.00		NIST
Inp	1015.00		NIST
Inp	1076.00		NIST
Inp	1076.00		NIST
Inp	1024.00		NIST
Inp	1024.00		NIST
Inp	1058.00		NIST
Inp	1051.00		NIST
Inp	1057.00		NIST
Inp	1068.00		NIST
Inp	1077.00		NIST
Inp	1053.00		NIST
Inp	1044.00		NIST
Inp	1044.00		NIST
Inp	1059.00		NIST
Inp	1030.00		NIST
Inp	1044.00		NIST
Inp	1050.00		NIST
Inp	1037.00		NIST
Inp	1040.00		NIST
Inp	1053.00		NIST
Inp	1066.00		NIST
Inp	1079.00		NIST
Inp	1065.00		NIST
Inp	1063.00		NIST
Inp	1030.00		NIST
Inp	1036.00		NIST
Inp	1035.00		NIST
Inp	1050.00		NIST
Inp	1055.00		NIST
Inp	1035.00		NIST
Inp	Outlier 170.20		NIST
Inp	Outlier 170.30		NIST
Inp	Outlier 172.54		NIST
Inp	Outlier 170.90		NIST
Inp	Outlier 171.30		NIST
Inp	Outlier 172.86		NIST
Inp	Outlier 172.86		NIST
Inp	Outlier 173.57		NIST
Inp	1035.00		NIST
Inp	Outlier 172.86		NIST
Inp	Outlier 170.20		NIST
I	[1959.00; 2053.00]
I	2004.00		NIST
I	1980.00		NIST
I	2014.00		NIST
I	1995.00		NIST
I	2022.00		NIST
I	2019.00		NIST
I	Outlier 1959.00		NIST
I	2011.00		NIST
I	2011.00		NIST
I	2000.00		NIST
I	2000.00		NIST
I	Outlier 1969.00		NIST
I	2000.00		NIST
I	2000.00		NIST
I	2019.80		NIST
I	2017.19		NIST
I	2020.19		NIST
I	2014.43		NIST
I	2033.00		NIST
I	2011.00		NIST
I	2012.00		NIST
I	2002.00		NIST
I	2000.00		NIST
I	2021.00		NIST
I	1992.00		NIST
I	1993.00		NIST
I	1992.00		NIST
I	2011.00		NIST
I	2030.00		NIST
I	2008.00		NIST
I	1995.00		NIST
I	Outlier 2050.00		NIST
I	2007.00		NIST
I	2025.00		NIST
I	2025.00		NIST
I	2010.00		NIST
I	2010.00		NIST
I	1980.00		NIST
I	2030.00		NIST
I	Outlier 2053.00		NIST
I	2012.00		NIST
I	1996.00		NIST
I	2000.00		NIST
I	1970.00		NIST
I	1979.00		NIST
I	1979.00		NIST
I	2014.00		NIST
I	2010.00		NIST
I	2012.00		NIST
I	1979.00		NIST
I	2004.00		NIST
I	2000.00		NIST
I	2011.00		NIST
I	2007.00		NIST
S°solid,1 bar	165.44	J/mol×K	NIST
Tboil	[460.90; 464.95]	K
Tboil	464.19	K	KDB
Tboil	464.20	K	NIST
Tboil	463.75 ± 2.00	K	NIST
Tboil	464.10 ± 0.30	K	NIST
Tboil	464.25 ± 1.00	K	NIST
Tboil	464.30 ± 0.60	K	NIST
Tboil	463.95 ± 1.00	K	NIST
Tboil	464.25 ± 0.30	K	NIST
Tboil	464.25 ± 0.35	K	NIST
Tboil	Outlier 460.90 ± 0.70	K	NIST
Tboil	464.95 ± 1.50	K	NIST
Tboil	464.65 ± 1.50	K	NIST
Tboil	464.15 ± 0.50	K	NIST
Tc	[695.15; 697.60]	K
Tc	697.60	K	KDB
Tc	697.60 ± 0.40	K	NIST
Tc	697.55 ± 0.23	K	NIST
Tc	695.15 ± 2.00	K	NIST
Tc	695.50 ± 3.00	K	NIST
Tfus	[302.55; 304.60]	K
Tfus	304.15	K	Liquid pharmaceuticals formulation by eutectic formation
Tfus	302.90	K	KDB
Tfus	304.60	K	Aq. Solubility Prediction
Tfus	304.00 ± 0.30	K	NIST
Tfus	304.14 ± 0.05	K	NIST
Tfus	304.05 ± 0.30	K	NIST
Tfus	304.09 ± 0.05	K	NIST
Tfus	304.09 ± 0.10	K	NIST
Tfus	303.55 ± 0.25	K	NIST
Tfus	303.50 ± 0.20	K	NIST
Tfus	303.55 ± 0.50	K	NIST
Tfus	303.70 ± 0.50	K	NIST
Tfus	302.65 ± 0.40	K	NIST
Tfus	303.45 ± 0.40	K	NIST
Tfus	303.75 ± 0.20	K	NIST
Tfus	303.60 ± 0.30	K	NIST
Tfus	302.55 ± 0.50	K	NIST
Tfus	302.90 ± 0.15	K	NIST
Ttriple	[304.20; 304.20]	K
Ttriple	304.20 ± 0.02	K	NIST
Ttriple	304.20 ± 0.02	K	NIST
Vc	0.282	m3/kmol	KDB
Zc	0.2435810		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[225.90; 233.60]	J/mol×K	[283.00; 313.00]
Cp,liquid	225.90	J/mol×K	283.00	NIST
Cp,liquid	233.60	J/mol×K	313.00	NIST
Cp,solid	154.56	J/mol×K	298.15	NIST
η	[0.0055660; 0.0132800]	Pa×s	[288.15; 308.15]
η	0.0132800	Pa×s	288.15	Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η	0.0096800	Pa×s	293.15	Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η	0.0077600	Pa×s	298.15	Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η	0.0065750	Pa×s	303.15	Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η	0.0055660	Pa×s	308.15	Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
ΔfusH	[13.94; 15.90]	kJ/mol	[303.00; 305.40]
ΔfusH	13.94	kJ/mol	303.00	NIST
ΔfusH	14.80	kJ/mol	304.05	NIST
ΔfusH	15.90	kJ/mol	304.10	NIST
ΔfusH	14.80	kJ/mol	304.10	NIST
ΔfusH	15.82	kJ/mol	304.20	NIST
ΔfusH	15.82	kJ/mol	304.20	NIST
ΔfusH	15.82	kJ/mol	304.20	NIST
ΔfusH	15.82	kJ/mol	304.20	NIST
ΔfusH	14.80	kJ/mol	305.40	NIST
ΔsubH	[74.80; 76.00]	kJ/mol	[288.00; 288.00]
ΔsubH	74.80	kJ/mol	288.00	NIST
ΔsubH	76.00 ± 0.80	kJ/mol	288.00	NIST
ΔvapH	[44.00; 58.50]	kJ/mol	[356.50; 573.50]
ΔvapH	58.50	kJ/mol	356.50	NIST
ΔvapH	51.30	kJ/mol	428.00	NIST
ΔvapH	50.10	kJ/mol	434.50	NIST
ΔvapH	48.20	kJ/mol	438.50	NIST
ΔvapH	45.19	kJ/mol	464.10	KDB
ΔvapH	46.20	kJ/mol	494.50	NIST
ΔvapH	44.00	kJ/mol	573.50	NIST
n0	[1.53699; 1.54680]		[293.15; 308.15]
n0	1.54670		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0	1.54680		293.15	Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
n0	1.54680		298.15	Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
n0	1.54670		298.15	Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
n0	1.54400		298.15	Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
n0	1.54099		303.15	Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
n0	1.53860		308.15	Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
n0	1.53699		308.15	Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
ρl	[1001.46; 1046.00]	kg/m3	[293.15; 343.15]
ρl	1045.77	kg/m3	293.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1046.00	kg/m3	293.15	Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
ρl	1041.41	kg/m3	298.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1036.94	kg/m3	303.15	Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
ρl	1037.05	kg/m3	303.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1037.02	kg/m3	303.15	Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl	1032.58	kg/m3	308.15	Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl	1032.73	kg/m3	308.15	Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
ρl	1032.73	kg/m3	308.15	Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
ρl	1032.64	kg/m3	308.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1028.00	kg/m3	313.00	KDB
ρl	1028.19	kg/m3	313.15	Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl	1028.25	kg/m3	313.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1023.82	kg/m3	318.15	Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl	1023.83	kg/m3	318.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1019.39	kg/m3	323.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1018.80	kg/m3	323.20	Liquid-liquid equilibrium for methyl butyl ketone + o-, m-, p-cresol + water ternary systems and COSMO-SAC predictions
ρl	1014.93	kg/m3	328.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1010.46	kg/m3	333.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1005.97	kg/m3	338.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1001.46	kg/m3	343.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ΔfusS	[46.00; 52.00]	J/mol×K	[303.00; 304.20]
ΔfusS	46.00	J/mol×K	303.00	NIST
ΔfusS	49.00	J/mol×K	304.05	NIST
ΔfusS	52.00	J/mol×K	304.20	NIST
ΔfusS	52.00	J/mol×K	304.20	NIST
γ	0.03	N/m	333.20	KDB

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	411.26	K	20.00	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.20	1022.00	1027.5
313.20	2031.00	1028.1
313.20	3017.00	1028.7
313.20	4012.00	1029.2
313.20	5018.00	1029.8
313.20	6010.00	1030.4
313.20	7005.00	1030.9
313.20	8006.00	1031.5
313.20	9004.00	1032.0
313.20	10005.00	1032.6
323.16	1013.00	1018.7
323.16	2039.00	1019.3
323.16	3007.00	1019.9
323.16	4009.00	1020.5
323.16	5005.00	1021.1
323.16	6004.00	1021.7
323.16	6999.00	1022.2
323.16	8008.00	1022.8
323.16	9002.00	1023.4
323.16	10005.00	1024.0
333.10	1010.00	1009.9
333.10	2033.00	1010.5
333.10	3009.00	1011.1
333.10	4014.00	1011.8
333.10	5004.00	1012.4
333.10	5998.00	1013.0
333.10	7000.00	1013.6
333.10	8009.00	1014.2
333.10	9004.00	1014.8
333.10	10010.00	1015.4
343.06	1023.00	1000.8
343.06	2024.00	1001.6
343.06	3015.00	1002.2
343.06	4003.00	1002.9
343.06	5009.00	1003.6
343.06	6005.00	1004.2
343.06	7008.00	1004.8
343.06	8003.00	1005.5
343.06	8999.00	1006.1
343.06	10004.00	1006.7
352.99	1043.00	991.9
352.99	2000.00	992.6
352.99	3034.00	993.3
352.99	4015.00	994.0
352.99	5033.00	994.6
352.99	6007.00	995.3
352.99	7016.00	996.0
352.99	8006.00	996.7
352.99	9015.00	997.3
352.99	10014.00	998.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[113.61; 284.36]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-4.63000e+01
Coefficient B			7.44520e-01
Coefficient C			-6.44560e-04
Coefficient D			2.30700e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	113.61	J/mol×K	273.00	Calculated Property
Cp,gas	146.64	J/mol×K	353.78	Calculated Property
Cp,gas	174.45	J/mol×K	434.56	Calculated Property
Cp,gas	197.77	J/mol×K	515.33	Calculated Property
Cp,gas	217.34	J/mol×K	596.11	Calculated Property
Cp,gas	233.88	J/mol×K	676.89	Calculated Property
Cp,gas	248.12	J/mol×K	757.67	Calculated Property
Cp,gas	260.80	J/mol×K	838.44	Calculated Property
Cp,gas	272.63	J/mol×K	919.22	Calculated Property
Cp,gas	284.36	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[352.96; 491.67]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46886e+01
Coefficient B			-3.72850e+03
Coefficient C			-9.40520e+01
Temperature range, min.			352.96
Temperature range, max.			491.67
Pvap	1.33	kPa	352.96	Calculated Property
Pvap	2.99	kPa	368.37	Calculated Property
Pvap	6.17	kPa	383.78	Calculated Property
Pvap	11.82	kPa	399.20	Calculated Property
Pvap	21.27	kPa	414.61	Calculated Property
Pvap	36.26	kPa	430.02	Calculated Property
Pvap	59.00	kPa	445.43	Calculated Property
Pvap	92.16	kPa	460.85	Calculated Property
Pvap	138.85	kPa	476.26	Calculated Property
Pvap	202.65	kPa	491.67	Calculated Property
Pvap	[0.06; 5016.43]	kPa	[304.19; 697.55]	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			1.36184e+02
Coefficient B			-1.20881e+04
Coefficient C			-1.74841e+01
Coefficient D			8.51800e-06
Coefficient E			0.00000e+00
Temperature range, min.			304.19
Temperature range, max.			697.55
Pvap	0.06	kPa	304.19	Calculated Property
Pvap	1.17	kPa	347.90	Calculated Property
Pvap	9.37	kPa	391.60	Calculated Property
Pvap	44.45	kPa	435.31	Calculated Property
Pvap	147.77	kPa	479.02	Calculated Property
Pvap	384.51	kPa	522.72	Calculated Property
Pvap	843.73	kPa	566.43	Calculated Property
Pvap	1644.20	kPa	610.14	Calculated Property
Pvap	2952.18	kPa	653.84	Calculated Property
Pvap	5016.43	kPa	697.55	Calculated Property
Pvap	[10.13; 101.22]	kPa	[393.37; 464.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37413e+01
Coefficient B			-3.20366e+03
Coefficient C			-1.12974e+02
Reference			Dreisbach and Shrader, 1949
Temperature range, min.			393.37
Temperature range, max.			464.10
Pvap	10.13	kPa	393.37	Calculated Property
Pvap	13.84	kPa	401.23	Calculated Property
Pvap	18.58	kPa	409.09	Calculated Property
Pvap	24.58	kPa	416.95	Calculated Property
Pvap	32.06	kPa	424.81	Calculated Property
Pvap	41.27	kPa	432.66	Calculated Property
Pvap	52.49	kPa	440.52	Calculated Property
Pvap	66.00	kPa	448.38	Calculated Property
Pvap	82.14	kPa	456.24	Calculated Property
Pvap	101.22	kPa	464.10	Calculated Property

Similar Compounds

Find more compounds similar to Phenol, 2-methyl-.

Mixtures

• Phenol, 2-methyl- + Formamide, N,N-dimethyl-
• Phenol, 2-methyl- + Benzene, ethyl-
• 3-Penten-2-one, 4-methyl- + Phenol, 2-methyl- + Water
• Phenol, 2-methyl- + Choline chloride
• Phenol, 2-methyl- + 2-Hexanone + Water
• Phenol, 2-methyl- + 1,2-Ethanediol + Heptane
• Methyl Isobutyl Ketone + Phenol, 2-methyl- + Water
• Phenol, 2-methyl- + Ethanol
• Phenol, 2-methyl- + Toluene + 1,2-Ethanediol
• Phenol, 2-methyl- + Ethane, 1,2-dichloro-
• Trichloroethylene + Phenol, 2-methyl-
• Phenol, 2-methyl- + o-Xylene
• Phenol, 2-methyl- + p-Xylene
• Phenol, 2-methyl- + Ethane, 1,1,2,2-tetrachloro-
• Phenol, 2-methyl- + Tetrachloroethylene
• Phenol, 2-methyl- + Benzene, 1,3-dimethyl-
• Phenol, 2-methyl- + Heptane
• Phenol, 2-methyl- + Water
• Phenol, 2-methyl- + Methyl Alcohol
• 1-Propanol + Phenol, 2-methyl-

Find more mixtures with Phenol, 2-methyl-.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
• Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
• Liquid-liquid equilibria in the ternary systems water + cresols + methyl butyl ketone at 298.2 and 313.2 K: experimental data and correlation
• Measurement of infinite dilution partition coefficients of isomeric benzene derivatives in [bmim][Tf2N]-CO2 biphasic system and correlation with the ePC-SAFT equation of state
• Liquid-liquid equilibria for the extraction of phenols from alkane using ethylene glycol
• Liquid-liquid equilibria for methyl isobutyl ketone + cresols + water at 333.15K, 343.15K and 353.15K: Experimental results and data correlation
• Determination and modeling of liquid-liquid equilibrium for ternary mixtures of methyl isopropyl ketone, cresol isomers and water
• Measurement, correlation and COSMO-SAC prediction of liquid-liquid equilibrium for the ternary systems, mesityl oxide + o-, m-, p-cresol + water, at 333.2 K and 353.2 K
• Liquid pharmaceuticals formulation by eutectic formation
• Phase equilibria of phenolic compounds in water or ethanol
• Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
• Heat capacities of aqueous polar aromatic compounds over a wide range of conditions. Part I: phenol, cresols, aniline, and toluidines
• Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
• Volumetric and ultrasonic behaviour of binary mixtures of 1-nonanol with o-cresol, m-cresol, p-cresol and anisole at T = (293.15 and 313.15) K
• Excess parameters of binary mixtures of anisaldehyde with o-cresol, m-cresol and p-cresol at T = (303.15, 308.15, 313.15, and 318.15) K
• Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of o-cresol, m-cresol or p-cresol from aqueous solution with 2-pentanone
• Liquid-liquid equilibria for toluene/heptane + phenol/cresols + ethylene glycol system
• Extraction of o-, m- and p-cresol from aqueous solution with methyl isopropyl ketone: Equilibrium, correlations, and COSMO-RS predictions
• Liquid-liquid equilibrium for methyl butyl ketone + o-, m-, p-cresol + water ternary systems and COSMO-SAC predictions
• Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
• Thermochemistry of Li, Na, K, Rb and Cs alkylated phenoxides
• Liquid Liquid Equilibrium for the Ternary Systems Methyl tert-Butyl Ketone + o-, m-, p-Cresol + Water at (298.2, 313.2, and 323.2) K
• Phase Equilibrium on Extraction Methylphenols from Aqueous Solution with 3,3-Dimethyl-2-butanone at 333.2 K and 353.2 K
• Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
• Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
• Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
• Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
• Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
• Formation of Deep Eutectic Solvents by Phenols and Choline Chloride and Their Physical Properties
• Densities of Cresols and Linear Alkane Mixtures at High Pressure
• Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
• Experimental Determination and Correlation of Liquid Liquid Equilibria for the Ternary System 2-Methoxy-2-methylpropane + o-Cresol + Water at 298.15 K and 313.15 K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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