Chemical Properties of Phenol, 2,6-dimethyl- (CAS 576-26-1)

InChI

InChI=1S/C8H10O/c1-6-4-3-5-7(2)8(6)9/h3-5,9H,1-2H3

InChI Key

NXXYKOUNUYWIHA-UHFFFAOYSA-N

Formula

C8H10O

SMILES

Cc1cccc(C)c1O

Molecular Weight¹

122.16

CAS

576-26-1

Other Names

• 1,2,6-Xylenol
• 1,3-Dimethyl-2-hydroxybenzene
• 1-hydroxy-2,6-dimethylbenzene
• 2,6-Dmp
• 2,6-dimethylphenol
• 2,6-xylenol
• NSC 2123

• ω : Acentric Factor.
• 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).
• 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_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).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (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.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4395; 0.4554]
ω	0.4395		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4554		ChemSep v8.3 pure component data Compiled value
ΔcH°solid	[-4344.20; -4325.40]	kJ/mol
ΔcH°solid	-4344.20 ± 2.90	kJ/mol	NIST
ΔcH°solid	-4325.40	kJ/mol	NIST
ΔcH°solid	-4339.90 ± 1.00	kJ/mol	NIST
μ	1.41	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-39.04	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-174.40; -157.50]	kJ/mol
ΔfH°gas	-161.75	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-161.90	kJ/mol	KDB
ΔfH°gas	-157.50	kJ/mol	NIST
ΔfH°gas	-174.40	kJ/mol	NIST
ΔfH°gas	-161.80 ± 0.54	kJ/mol	NIST
ΔfH°solid	[-250.00; -233.10]	kJ/mol
ΔfH°solid	-233.10 ± 2.90	kJ/mol	NIST
ΔfH°solid	-250.00	kJ/mol	NIST
ΔfH°solid	-237.40 ± 1.10	kJ/mol	NIST
ΔfusH°	15.91	kJ/mol	Joback Calculated Property
ΔsubH°	[59.40; 75.60]	kJ/mol
ΔsubH°	75.60	kJ/mol	NIST
ΔsubH°	75.10	kJ/mol	NIST
ΔsubH°	75.60 ± 0.20	kJ/mol	NIST
ΔsubH°	75.60	kJ/mol	NIST
ΔsubH°	Outlier 59.40 ± 0.80	kJ/mol	NIST
ΔsubH°	75.10	kJ/mol	NIST
ΔvapH°	[75.10; 75.60]	kJ/mol
ΔvapH°	75.31	kJ/mol	NIST
ΔvapH°	75.60	kJ/mol	NIST
ΔvapH°	75.10	kJ/mol	NIST
IE	[8.05; 8.34]	eV
IE	8.05 ± 0.02	eV	NIST
IE	8.26	eV	NIST
IE	8.34	eV	NIST
log10WS	[-1.31; -1.29]
log10WS	-1.31		Aq. Solubility Prediction
log10WS	-1.29		Estimated Solubility
logPoct/wat	2.009		Crippen Calculated Property
McVol	105.690	ml/mol	McGowan Calculated Property
Pc	[4255.65; 4255.65]	kPa
Pc	4255.65	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4255.65	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	0.17	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[182.30; 1138.00]
Inp	1098.00		NIST
Inp	1115.77		NIST
Inp	1080.49		NIST
Inp	1081.07		NIST
Inp	1081.55		NIST
Inp	1082.02		NIST
Inp	1079.00		NIST
Inp	1083.07		NIST
Inp	1087.90		NIST
Inp	1097.00		NIST
Inp	1100.00		NIST
Inp	1090.00		NIST
Inp	1096.00		NIST
Inp	1084.10		NIST
Inp	1096.00		NIST
Inp	1100.00		NIST
Inp	1138.00		NIST
Inp	1098.00		NIST
Inp	1102.30		NIST
Inp	1104.60		NIST
Inp	1105.50		NIST
Inp	1080.50		NIST
Inp	1080.00		NIST
Inp	1102.30		NIST
Inp	1104.60		NIST
Inp	1105.50		NIST
Inp	1108.00		NIST
Inp	1082.12		NIST
Inp	1077.41		NIST
Inp	1078.00		NIST
Inp	1078.41		NIST
Inp	1130.00		NIST
Inp	1117.00		NIST
Inp	1114.20		NIST
Inp	1114.90		NIST
Inp	1117.20		NIST
Inp	1130.00		NIST
Inp	1090.00		NIST
Inp	1080.00		NIST
Inp	1079.00		NIST
Inp	1105.00		NIST
Inp	1128.00		NIST
Inp	1093.00		NIST
Inp	1106.31		NIST
Inp	1076.00		NIST
Inp	1087.00		NIST
Inp	1108.00		NIST
Inp	1111.00		NIST
Inp	1112.00		NIST
Inp	1098.00		NIST
Inp	1105.00		NIST
Inp	1108.00		NIST
Inp	1079.00		NIST
Inp	1078.00		NIST
Inp	Outlier 184.51		NIST
Inp	Outlier 182.30		NIST
Inp	Outlier 184.08		NIST
Inp	Outlier 184.08		NIST
Inp	Outlier 184.51		NIST
Inp	1115.77		NIST
Inp	1079.00		NIST
Inp	1100.00		NIST
Inp	1096.00		NIST
Inp	1087.00		NIST
Inp	1112.00		NIST
Inp	1078.00		NIST
Ip	[1889.00; 1918.00]
Ip	1917.00		NIST
Ip	1918.00		NIST
Ip	1894.00		NIST
Ip	1889.00		NIST
Ip	1894.00		NIST
Ip	1917.00		NIST
Tboil	[472.65; 476.20]	K
Tboil	474.35	K	Experimental and Predicted Vapor-Liquid Equilibrium for Diisopropanolamine with m-Cresol and 2,6-Dimethylphenol at 20.0 kPa
Tboil	474.18	K	ChemSep v8.3 pure component data Compiled value
Tboil	474.22	K	KDB
Tboil	Outlier 476.20	K	NIST
Tboil	474.15 ± 2.00	K	NIST
Tboil	474.15 ± 2.00	K	NIST
Tboil	474.55 ± 2.00	K	NIST
Tboil	473.75 ± 2.00	K	NIST
Tboil	472.65 ± 5.00	K	NIST
Tboil	474.55 ± 2.00	K	NIST
Tc	[700.95; 701.00]	K
Tc	701.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	701.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	700.95	K	ChemSep v8.3 pure component data Compiled value
Tc	701.00	K	KDB
Tc	700.95 ± 0.20	K	NIST
Tfus	[310.65; 322.15]	K
Tfus	320.65	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	318.77	K	ChemSep v8.3 pure component data Compiled value
Tfus	318.80	K	KDB
Tfus	320.57	K	Aq. Solubility Prediction
Tfus	318.45 ± 0.30	K	NIST
Tfus	318.77 ± 0.05	K	NIST
Tfus	321.15 ± 2.00	K	NIST
Tfus	319.25 ± 1.00	K	NIST
Tfus	317.65 ± 0.50	K	NIST
Tfus	317.90 ± 2.00	K	NIST
Tfus	319.60 ± 1.00	K	NIST
Tfus	321.15 ± 2.00	K	NIST
Tfus	322.15 ± 2.00	K	NIST
Tfus	Outlier 310.65 ± 7.00	K	NIST
Tfus	318.65 ± 1.00	K	NIST
Tfus	322.15 ± 2.00	K	NIST
Tfus	321.15 ± 2.00	K	NIST
Tfus	318.15 ± 2.00	K	NIST
Ttriple	318.76	K	ChemSep v8.3 pure component data Compiled value
UQi	3.82		ChemSep v8.3 pure component data Compiled value
URi	5.02		ChemSep v8.3 pure component data Compiled value
Vc	0.387	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Zc	0.2880000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔfusH	[18.83; 18.90]	kJ/mol	[318.60; 318.90]
ΔfusH	18.83	kJ/mol	318.60	NIST
ΔfusH	18.90	kJ/mol	318.90	NIST
ΔfusH	18.90	kJ/mol	318.90	NIST
ΔfusH	18.90	kJ/mol	318.90	NIST
ΔsubH	75.60 ± 0.17	kJ/mol	295.00	NIST
ΔvapH	48.50	kJ/mol	446.50	NIST
ΔfusS	59.26	J/mol×K	318.90	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[390.06; 438.90]	K	[6.70; 35.64]
Tboil(P)	390.06	K	6.70	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	396.14	K	8.87	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	401.43	K	10.89	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	405.64	K	12.74	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	409.97	K	14.98	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	413.33	K	16.80	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	416.65	K	18.91	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	418.11	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
Tboil(P)	419.43	K	21.02	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	422.01	K	22.83	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	436.55	K	33.02	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Tboil(P)	438.90	K	35.64	Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[134.09; 388.83]	J/mol×K	[255.00; 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			7.18220e+01
Coefficient B			-5.00000e+02
Coefficient C			6.09224e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	134.09	J/mol×K	255.00	Calculated Property
Cp,gas	195.92	J/mol×K	393.33	Calculated Property
Cp,gas	244.57	J/mol×K	531.67	Calculated Property
Cp,gas	281.58	J/mol×K	670.00	Calculated Property
Cp,gas	310.16	J/mol×K	808.33	Calculated Property
Cp,gas	332.71	J/mol×K	946.67	Calculated Property
Cp,gas	350.88	J/mol×K	1085.00	Calculated Property
Cp,gas	365.81	J/mol×K	1223.33	Calculated Property
Cp,gas	378.27	J/mol×K	1361.67	Calculated Property
Cp,gas	388.83	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[235.96; 312.92]	J/mol×K	[350.53; 520.53]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			7.72800e+01
Coefficient B			4.52700e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			350.53
Temperature range, max.			520.53
Cp,liquid	235.96	J/mol×K	350.53	Calculated Property
Cp,liquid	244.52	J/mol×K	369.42	Calculated Property
Cp,liquid	253.07	J/mol×K	388.31	Calculated Property
Cp,liquid	261.62	J/mol×K	407.20	Calculated Property
Cp,liquid	270.17	J/mol×K	426.09	Calculated Property
Cp,liquid	278.72	J/mol×K	444.97	Calculated Property
Cp,liquid	287.27	J/mol×K	463.86	Calculated Property
Cp,liquid	295.82	J/mol×K	482.75	Calculated Property
Cp,liquid	304.37	J/mol×K	501.64	Calculated Property
Cp,liquid	312.92	J/mol×K	520.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0066896; 0.0003607]	Pa×s	[318.76; 474.22]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-6.94020e+01
Coefficient B			5.91160e+03
Coefficient C			7.95380e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			318.76
Temperature range, max.			474.22
η	0.0066896	Pa×s	318.76	Calculated Property
η	0.0039235	Pa×s	336.03	Calculated Property
η	0.0024734	Pa×s	353.31	Calculated Property
η	0.0016575	Pa×s	370.58	Calculated Property
η	0.0011703	Pa×s	387.85	Calculated Property
η	0.0008641	Pa×s	405.13	Calculated Property
η	0.0006632	Pa×s	422.40	Calculated Property
η	0.0005264	Pa×s	439.67	Calculated Property
η	0.0004302	Pa×s	456.95	Calculated Property
η	0.0003607	Pa×s	474.22	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[54.68; 0.00]	kJ/mol	[318.76; 700.95]	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			6.78220e+01
Coefficient B			3.55260e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.00950e+02
Comment			Range stopped at Tc; ChemSep gives it to 701.05 K.
Temperature range, min.			318.76
Temperature range, max.			700.95
ΔvapH	54.68	kJ/mol	318.76	Calculated Property
ΔvapH	52.43	kJ/mol	361.23	Calculated Property
ΔvapH	50.01	kJ/mol	403.69	Calculated Property
ΔvapH	47.34	kJ/mol	446.16	Calculated Property
ΔvapH	44.37	kJ/mol	488.62	Calculated Property
ΔvapH	40.99	kJ/mol	531.09	Calculated Property
ΔvapH	37.01	kJ/mol	573.55	Calculated Property
ΔvapH	32.04	kJ/mol	616.02	Calculated Property
ΔvapH	25.05	kJ/mol	658.48	Calculated Property
ΔvapH	0.00	kJ/mol	700.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[359.38; 501.45]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.54388e+01
Coefficient B			-4.33921e+03
Coefficient C			-7.29830e+01
Temperature range, min.			359.38
Temperature range, max.			501.45
Pvap	1.33	kPa	359.38	Calculated Property
Pvap	2.94	kPa	375.17	Calculated Property
Pvap	6.00	kPa	390.95	Calculated Property
Pvap	11.45	kPa	406.74	Calculated Property
Pvap	20.59	kPa	422.52	Calculated Property
Pvap	35.20	kPa	438.31	Calculated Property
Pvap	57.58	kPa	454.09	Calculated Property
Pvap	90.56	kPa	469.88	Calculated Property
Pvap	137.57	kPa	485.66	Calculated Property
Pvap	202.66	kPa	501.45	Calculated Property
Pvap	[0.17; 4316.33]	kPa	[318.76; 700.95]	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			1.22422e+02
Coefficient B			-1.12900e+04
Coefficient C			-1.55460e+01
Coefficient D			7.97590e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 701.05 K.
Temperature range, min.			318.76
Temperature range, max.			700.95
Pvap	0.17	kPa	318.76	Calculated Property
Pvap	1.92	kPa	361.23	Calculated Property
Pvap	11.81	kPa	403.69	Calculated Property
Pvap	47.65	kPa	446.16	Calculated Property
Pvap	143.49	kPa	488.62	Calculated Property
Pvap	351.99	kPa	531.09	Calculated Property
Pvap	746.83	kPa	573.55	Calculated Property
Pvap	1429.81	kPa	616.02	Calculated Property
Pvap	2546.71	kPa	658.48	Calculated Property
Pvap	4316.33	kPa	700.95	Calculated Property
Pvap	[0.16; 4387.97]	kPa	[318.76; 701.05]	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			1.30489e+02
Coefficient B			-1.16579e+04
Coefficient C			-1.67611e+01
Coefficient D			8.86220e-06
Coefficient E			0.00000e+00
Temperature range, min.			318.76
Temperature range, max.			701.05
Pvap	0.16	kPa	318.76	Calculated Property
Pvap	1.93	kPa	361.24	Calculated Property
Pvap	11.92	kPa	403.71	Calculated Property
Pvap	47.95	kPa	446.19	Calculated Property
Pvap	143.89	kPa	488.67	Calculated Property
Pvap	352.04	kPa	531.14	Calculated Property
Pvap	746.51	kPa	573.62	Calculated Property
Pvap	1432.39	kPa	616.10	Calculated Property
Pvap	2565.43	kPa	658.57	Calculated Property
Pvap	4387.97	kPa	701.05	Calculated Property
Pvap	[19.85; 107.75]	kPa	[418.00; 476.67]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42978e+01
Coefficient B			-3.77268e+03
Coefficient C			-8.44160e+01
Reference			Andon, Biddiscombe, et al., 1960
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			418.00
Temperature range, max.			476.67
Pvap	19.85	kPa	418.00	Calculated Property
Pvap	24.66	kPa	424.52	Calculated Property
Pvap	30.38	kPa	431.04	Calculated Property
Pvap	37.13	kPa	437.56	Calculated Property
Pvap	45.07	kPa	444.08	Calculated Property
Pvap	54.32	kPa	450.59	Calculated Property
Pvap	65.05	kPa	457.11	Calculated Property
Pvap	77.41	kPa	463.63	Calculated Property
Pvap	91.59	kPa	470.15	Calculated Property
Pvap	107.75	kPa	476.67	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[891.35; 345.54]	kg/m3	[318.76; 700.95]	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			9.01216e+01
Coefficient B			2.88000e-01
Coefficient C			7.01050e+02
Coefficient D			2.85710e-01
Comment			Range stopped at Tc; ChemSep gives it to 701.05 K.
Temperature range, min.			318.76
Temperature range, max.			700.95
ρl	891.35	kg/m3	318.76	Calculated Property
ρl	861.01	kg/m3	361.23	Calculated Property
ρl	829.00	kg/m3	403.69	Calculated Property
ρl	794.94	kg/m3	446.16	Calculated Property
ρl	758.21	kg/m3	488.62	Calculated Property
ρl	717.90	kg/m3	531.09	Calculated Property
ρl	672.40	kg/m3	573.55	Calculated Property
ρl	618.47	kg/m3	616.02	Calculated Property
ρl	547.32	kg/m3	658.48	Calculated Property
ρl	345.54	kg/m3	700.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[318.76; 700.95]	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 γ in N/m, T in K
Coefficient A			5.84880e-02
Coefficient B			1.16870e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.00950e+02
Comment			Range stopped at Tc; ChemSep gives it to 701.05 K.
Temperature range, min.			318.76
Temperature range, max.			700.95
γ	0.03	N/m	318.76	Calculated Property
γ	0.03	N/m	361.23	Calculated Property
γ	0.02	N/m	403.69	Calculated Property
γ	0.02	N/m	446.16	Calculated Property
γ	0.01	N/m	488.62	Calculated Property
γ	0.01	N/m	531.09	Calculated Property
γ	0.01	N/m	573.55	Calculated Property
γ	0.00	N/m	616.02	Calculated Property
γ	0.00	N/m	658.48	Calculated Property
γ	0.00	N/m	700.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.07]	W/m×K	[474.22; 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			1.98600e-04
Coefficient B			9.31400e-01
Coefficient C			7.17400e+02
Coefficient D			0.00000e+00
Temperature range, min.			474.22
Temperature range, max.			1000.00
λgas	0.02	W/m×K	474.22	Calculated Property
λgas	0.03	W/m×K	532.64	Calculated Property
λgas	0.03	W/m×K	591.06	Calculated Property
λgas	0.04	W/m×K	649.48	Calculated Property
λgas	0.04	W/m×K	707.90	Calculated Property
λgas	0.05	W/m×K	766.32	Calculated Property
λgas	0.06	W/m×K	824.74	Calculated Property
λgas	0.06	W/m×K	883.16	Calculated Property
λgas	0.07	W/m×K	941.58	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[318.76; 560.32]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.27790e-01
Coefficient B			-2.36420e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			318.76
Temperature range, max.			560.32
λliquid	0.15	W/m×K	318.76	Calculated Property
λliquid	0.15	W/m×K	345.60	Calculated Property
λliquid	0.14	W/m×K	372.44	Calculated Property
λliquid	0.13	W/m×K	399.28	Calculated Property
λliquid	0.13	W/m×K	426.12	Calculated Property
λliquid	0.12	W/m×K	452.96	Calculated Property
λliquid	0.11	W/m×K	479.80	Calculated Property
λliquid	0.11	W/m×K	506.64	Calculated Property
λliquid	0.10	W/m×K	533.48	Calculated Property
λliquid	0.10	W/m×K	560.32	Calculated Property

Similar Compounds

Find more compounds similar to Phenol, 2,6-dimethyl-.

Mixtures

• Phenol, 3-methyl- + Phenol, 2,6-dimethyl-
• Phenol, 2-methyl- + Phenol, 2,6-dimethyl-
• Diisopropanolamine + Phenol, 2,6-dimethyl-

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).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
• Thermochemistry of Li, Na, K, Rb and Cs alkylated phenoxides
• Experimental and Predicted Vapor-Liquid Equilibrium for Diisopropanolamine with m-Cresol and 2,6-Dimethylphenol at 20.0 kPa
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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