Chemical Properties of Anisole (CAS 100-66-3)

InChI

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

InChI Key

RDOXTESZEPMUJZ-UHFFFAOYSA-N

Formula

C7H8O

SMILES

COc1ccccc1

Molecular Weight¹

108.14

CAS

100-66-3

Other Names

• Anizol
• Benzene, methoxy-
• Ether, methyl phenyl-
• NSC 7920
• UN 2222
• anisol
• methoxybenzene
• methyl phenyl ether
• phenoxymethane
• phenyl methyl ether

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid 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).
• ε_r : Dielectric Constant (Relative permittivity).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion 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.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• 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_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3288; 0.3502]
ω	0.3288		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3502		ChemSep v8.3 pure component data Compiled value
PAff	839.60	kJ/mol	NIST
Tig	748.15	K	NCMS SOLV-DB
BasG	807.20	kJ/mol	NIST
ΔcH°liquid	[-3783.12; -3778.00]	kJ/mol
ΔcH°liquid	-3783.12	kJ/mol	NIST
ΔcH°liquid	-3778.00 ± 0.80	kJ/mol	NIST
ΔcH°liquid	-3779.50	kJ/mol	NIST
Cp,liquid	191.54	J/mol×K	Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
μ	1.36	debye	ChemSep v8.3 pure component data Compiled value
εr	4.33		NCMS SOLV-DB
Tflash,cc	325.15	K	NCMS SOLV-DB
ΔfG°	22.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-76.69; -67.90]	kJ/mol
ΔfH°gas	-68.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-67.90 ± 1.20	kJ/mol	NIST
ΔfH°gas	-76.69 ± 0.92	kJ/mol	NIST
ΔfH°gas	-70.70	kJ/mol	NIST
ΔfH°gas	-75.10	kJ/mol	NIST
ΔfH°liquid	[-120.00; -114.80]	kJ/mol
ΔfH°liquid	-114.80 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-120.00 ± 0.80	kJ/mol	NIST
ΔfH°liquid	-118.40	kJ/mol	NIST
ΔfusH°	9.12	kJ/mol	Joback Calculated Property
ΔvapH°	[38.00; 46.91]	kJ/mol
ΔvapH°	46.86	kJ/mol	NCMS SOLV-DB
ΔvapH°	46.91	kJ/mol	NIST
ΔvapH°	44.30	kJ/mol	NIST
ΔvapH°	46.60 ± 0.20	kJ/mol	NIST
ΔvapH°	45.30	kJ/mol	NIST
ΔvapH°	46.90	kJ/mol	NIST
ΔvapH°	46.84 ± 0.22	kJ/mol	NIST
ΔvapH°	46.90	kJ/mol	NIST
ΔvapH°	46.80 ± 0.20	kJ/mol	NIST
ΔvapH°	38.00 ± 0.40	kJ/mol	NIST
ΔvapH°	43.30	kJ/mol	NIST
ΔvapH°	38.20 ± 0.40	kJ/mol	NIST
ΔvapH°	39.40	kJ/mol	NIST
ΔvapH°	39.40	kJ/mol	NIST
IE	[8.10; 8.80]	eV
IE	8.20 ± 0.05	eV	NIST
IE	8.25 ± 0.03	eV	NIST
IE	8.10	eV	NIST
IE	8.24	eV	NIST
IE	8.60	eV	NIST
IE	8.20 ± 0.02	eV	NIST
IE	8.37	eV	NIST
IE	8.30 ± 0.10	eV	NIST
IE	8.20	eV	NIST
IE	8.18	eV	NIST
IE	Outlier 8.80 ± 0.10	eV	NIST
IE	8.40 ± 0.10	eV	NIST
IE	8.21	eV	NIST
IE	8.60	eV	NIST
IE	8.22 ± 0.02	eV	NIST
IE	8.20 ± 0.02	eV	NIST
IE	8.39	eV	NIST
IE	8.45	eV	NIST
IE	8.42	eV	NIST
IE	8.25	eV	NIST
IE	8.39	eV	NIST
IE	8.46	eV	NIST
IE	8.42	eV	NIST
log10WS	[-1.85; -1.85]
log10WS	-1.85		Aq. Solubility Prediction
log10WS	-1.85		Estimated Solubility
logPoct/wat	2.110		NCMS SOLV-DB
McVol	91.600	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[4174.59; 4250.00]	kPa
Pc	4240.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	4174.59	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4180.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4222.00 ± 20.00	kPa	NIST
Pc	4250.00 ± 100.00	kPa	NIST
Pc	4179.66 ± 202.65	kPa	NIST
Pc	4180.00 ± 60.79	kPa	NIST
Pc	4174.59 ± 101.32	kPa	NIST
Pc	4184.72 ± 101.32	kPa	NIST
Ptriple	2.45e-03	kPa	ChemSep v8.3 pure component data Compiled value
ρc	316.84 ± 9.95	kg/m3	NIST
Inp	[880.00; 956.00]
Inp	891.69		NIST
Inp	893.73		NIST
Inp	895.86		NIST
Inp	897.86		NIST
Inp	900.00		NIST
Inp	902.32		NIST
Inp	904.91		NIST
Inp	907.48		NIST
Inp	909.99		NIST
Inp	912.78		NIST
Inp	889.68		NIST
Inp	909.00		NIST
Inp	901.90		NIST
Inp	903.80		NIST
Inp	908.80		NIST
Inp	898.10		NIST
Inp	901.00		NIST
Inp	910.10		NIST
Inp	909.40		NIST
Inp	911.00		NIST
Inp	928.00		NIST
Inp	928.00		NIST
Inp	927.00		NIST
Inp	887.00		NIST
Inp	Outlier 880.00		NIST
Inp	900.00		NIST
Inp	927.00		NIST
Inp	915.00		NIST
Inp	916.00		NIST
Inp	919.00		NIST
Inp	935.00		NIST
Inp	940.00		NIST
Inp	913.00		NIST
Inp	930.00		NIST
Inp	930.00		NIST
Inp	923.60		NIST
Inp	920.00		NIST
Inp	898.40		NIST
Inp	918.00		NIST
Inp	915.00		NIST
Inp	923.00		NIST
Inp	900.30		NIST
Inp	893.90		NIST
Inp	908.00		NIST
Inp	907.00		NIST
Inp	906.00		NIST
Inp	902.00		NIST
Inp	Outlier 956.00		NIST
Inp	918.00		NIST
Inp	921.00		NIST
Inp	920.00		NIST
Inp	918.00		NIST
Inp	918.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	920.00		NIST
Inp	922.00		NIST
Inp	925.00		NIST
Inp	910.00		NIST
Inp	900.00		NIST
Inp	923.00		NIST
Inp	900.00		NIST
Inp	896.00		NIST
Inp	900.00		NIST
Inp	893.00		NIST
Inp	900.00		NIST
Inp	916.00		NIST
Inp	918.00		NIST
Inp	900.00		NIST
Inp	Outlier 956.00		NIST
Ip	[1306.00; 1398.00]
Ip	1340.00		NIST
Ip	1368.60		NIST
Ip	1340.00		NIST
Ip	1375.00		NIST
Ip	1373.00		NIST
Ip	1331.00		NIST
Ip	1368.60		NIST
Ip	Outlier 1394.00		NIST
Ip	Outlier 1398.00		NIST
Ip	1325.00		NIST
Ip	1354.00		NIST
Ip	1355.40		NIST
Ip	1345.60		NIST
Ip	1356.80		NIST
Ip	1353.80		NIST
Ip	1348.20		NIST
Ip	1351.00		NIST
Ip	1348.00		NIST
Ip	1350.90		NIST
Ip	1349.00		NIST
Ip	1342.00		NIST
Ip	1344.00		NIST
Ip	1341.00		NIST
Ip	1355.00		NIST
Ip	1355.00		NIST
Ip	1310.00		NIST
Ip	1327.00		NIST
Ip	1336.00		NIST
Ip	1327.00		NIST
Ip	1358.00		NIST
Ip	1327.00		NIST
Ip	Outlier 1306.00		NIST
Ip	1340.00		NIST
Ip	1327.00		NIST
Ip	1330.00		NIST
Ip	1341.00		NIST
Ip	1355.00		NIST
Tboil	[426.15; 428.20]	K
Tboil	426.56	K	Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
Tboil	426.69	K	Isobaric (vapour + liquid) equilibria of binary systems containing butyl acetate for the separation of methoxy aromatic compounds (anisole and guaiacol) from biomass fast pyrolysis oil
Tboil	426.77	K	Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
Tboil	426.95	K	ChemSep v8.3 pure component data Compiled value
Tboil	426.75	K	NCMS SOLV-DB
Tboil	427.20 ± 0.50	K	NIST
Tboil	Outlier 428.20	K	NIST
Tboil	427.00	K	NIST
Tboil	426.80	K	NIST
Tboil	427.05 ± 0.30	K	NIST
Tboil	426.65 ± 0.40	K	NIST
Tboil	426.90 ± 0.40	K	NIST
Tboil	426.15 ± 1.50	K	NIST
Tboil	426.90 ± 0.07	K	NIST
Tboil	426.80 ± 0.50	K	NIST
Tboil	426.64 ± 0.30	K	NIST
Tboil	427.00 ± 0.25	K	NIST
Tboil	Outlier 428.15 ± 1.50	K	NIST
Tboil	426.95 ± 0.25	K	NIST
Tboil	427.00 ± 0.50	K	NIST
Tboil	427.00 ± 0.50	K	NIST
Tboil	427.00 ± 0.50	K	NIST
Tboil	427.00 ± 0.40	K	NIST
Tboil	426.95 ± 0.30	K	NIST
Tc	[641.50; 647.40]	K
Tc	646.50	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	647.40	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	642.15	K	ChemSep v8.3 pure component data Compiled value
Tc	646.10 ± 0.20	K	NIST
Tc	644.10	K	NIST
Tc	645.60 ± 1.00	K	NIST
Tc	641.65 ± 2.00	K	NIST
Tc	641.50 ± 2.00	K	NIST
Tc	641.65 ± 1.50	K	NIST
Tfus	[235.20; 293.20]	K
Tfus	235.20	K	The solid-liquid equilitbrium, excess molar volume and refractive deviation properties of binary systems containing dimethyl carbonate, anisole and phenol
Tfus	236.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	235.85	K	ChemSep v8.3 pure component data Compiled value
Tfus	236.03	K	Aq. Solubility Prediction
Tfus	235.65	K	NCMS SOLV-DB
Tfus	268.73 ± 0.01	K	NIST
Tfus	235.75 ± 0.20	K	NIST
Tfus	235.65 ± 0.40	K	NIST
Tfus	235.77 ± 0.05	K	NIST
Tfus	236.04 ± 0.40	K	NIST
Tfus	235.95 ± 0.30	K	NIST
Tfus	235.65 ± 0.40	K	NIST
Tfus	235.95 ± 0.30	K	NIST
Tfus	Outlier 293.20 ± 1.00	K	NIST
Ttriple	235.65	K	ChemSep v8.3 pure component data Compiled value
UQi	3.21		ChemSep v8.3 pure component data Compiled value
URi	4.17		ChemSep v8.3 pure component data Compiled value
Vc	[0.337; 0.341]	m3/kmol
Vc	0.341	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.341	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.337	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	[0.2670000; 0.2690000]
Zc	0.2690000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc	0.2670000		ChemSep v8.3 pure component data Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[162.46; 195.94]	J/mol×K	[388.15; 498.15]
Cp,gas	162.46	J/mol×K	388.15	NIST
Cp,gas	168.82	J/mol×K	408.15	NIST
Cp,gas	176.98	J/mol×K	433.15	NIST
Cp,gas	183.05	J/mol×K	453.15	NIST
Cp,gas	188.99	J/mol×K	473.15	NIST
Cp,gas	195.94	J/mol×K	498.15	NIST
Cp,liquid	[191.20; 208.80]	J/mol×K	[297.20; 304.80]
Cp,liquid	191.20	J/mol×K	297.20	NIST
Cp,liquid	199.00	J/mol×K	298.15	NIST
Cp,liquid	208.80	J/mol×K	304.80	NIST
η	[0.0007890; 0.0011880]	Pa×s	[288.15; 303.15]
η	0.0011880	Pa×s	288.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η	0.0010840	Pa×s	293.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η	0.0010170	Pa×s	298.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η	0.0007890	Pa×s	298.15	NCMS SOLV-DB
η	0.0009310	Pa×s	303.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
ΔfusH	[11.66; 17.03]	kJ/mol	[236.00; 293.20]
ΔfusH	12.89	kJ/mol	236.00	NIST
ΔfusH	11.66	kJ/mol	237.00	NIST
ΔfusH	17.03	kJ/mol	293.20	NIST
ΔvapH	[38.90; 42.90]	kJ/mol	[359.50; 427.00]
ΔvapH	39.00	kJ/mol	359.50	NIST
ΔvapH	42.90 ± 0.10	kJ/mol	367.00	NIST
ΔvapH	42.00 ± 0.10	kJ/mol	382.00	NIST
ΔvapH	40.50 ± 0.10	kJ/mol	402.00	NIST
ΔvapH	41.80	kJ/mol	405.50	NIST
ΔvapH	41.90	kJ/mol	409.50	NIST
ΔvapH	41.90	kJ/mol	409.50	NIST
ΔvapH	38.97	kJ/mol	426.80	NIST
ΔvapH	38.90 ± 0.10	kJ/mol	427.00	NIST
Pvap	[0.02; 96.15]	kPa	[278.30; 424.79]
Pvap	0.12	kPa	278.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.15	kPa	281.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.19	kPa	284.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.23	kPa	287.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.29	kPa	290.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.35	kPa	293.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.41	kPa	296.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.02	kPa	298.15	NCMS SOLV-DB
Pvap	0.50	kPa	298.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.50	kPa	298.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.52	kPa	299.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.61	kPa	302.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.67	kPa	303.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.67	kPa	303.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.77	kPa	306.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.89	kPa	308.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.89	kPa	308.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.93	kPa	309.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	1.11	kPa	312.30	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	1.40	kPa	313.20	Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
Pvap	1.18	kPa	313.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	1.18	kPa	313.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	1.54	kPa	318.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	1.54	kPa	318.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	2.00	kPa	323.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	93.13	kPa	423.38	Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
Pvap	96.15	kPa	424.55	Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
Pvap	96.15	kPa	424.61	Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
Pvap	96.15	kPa	424.79	Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
n0	[1.50341; 1.52560]		[288.15; 318.15]
n0	1.52560		288.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.51710		293.13	Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Anisole
n0	1.51610		293.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.51710		293.15	Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
n0	1.51770		293.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
n0	1.51690		293.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.51720		293.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.51460		298.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.51420		298.15	(Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
n0	1.51530		298.15	Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
n0	1.51410		298.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.51495		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	1.51370		298.15	Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
n0	1.51480		298.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0	1.51400		298.15	NCMS SOLV-DB
n0	1.51420		298.15	(Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
n0	1.51360		298.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0	1.51410		298.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.51554		298.15	Isobaric Vapor-Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa
n0	1.51290		303.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.51395		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	1.51191		303.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.51130		303.15	Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
n0	1.51240		303.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0	1.51170		303.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.51120		303.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0	1.51240		303.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
n0	1.50950		308.15	Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
n0	1.50880		308.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0	1.50920		308.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0	1.51095		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
n0	1.50865		308.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.50880		308.15	Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
n0	1.50604		313.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0	1.50341		318.15	Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
ρl	[965.73; 1003.30]	kg/m3	[283.15; 323.15]
ρl	1003.30	kg/m3	283.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	996.56	kg/m3	288.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	998.62	kg/m3	288.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	994.01	kg/m3	293.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	991.95	kg/m3	293.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	993.60	kg/m3	298.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl	989.13	kg/m3	298.15	Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
ρl	989.32	kg/m3	298.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	989.32	kg/m3	298.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	989.42	kg/m3	298.15	Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
ρl	988.90	kg/m3	298.15	Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
ρl	989.13	kg/m3	298.15	Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
ρl	989.42	kg/m3	298.15	Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures
ρl	989.42	kg/m3	298.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	989.09	kg/m3	298.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	983.04	kg/m3	303.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	989.40	kg/m3	303.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl	984.59	kg/m3	303.15	The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl	984.40	kg/m3	303.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρl	979.80	kg/m3	308.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρl	980.04	kg/m3	308.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	979.50	kg/m3	308.15	Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
ρl	984.60	kg/m3	308.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl	978.34	kg/m3	308.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	975.25	kg/m3	313.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	975.00	kg/m3	313.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρl	973.62	kg/m3	313.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	980.00	kg/m3	313.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl	970.52	kg/m3	318.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl	970.50	kg/m3	318.15	Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
ρl	969.99	kg/m3	318.15	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
ρl	965.73	kg/m3	323.15	The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ΔfusS	58.10	J/mol×K	293.20	NIST
γ	0.04	N/m	298.15	NCMS SOLV-DB

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	989.2
298.15	10000.00	995.6
298.15	15000.00	998.5
298.15	20000.00	1001.4
298.15	25000.00	1004.1
298.15	30000.00	1006.9
298.15	35000.00	1009.7
298.15	40000.00	1012.5
298.15	45000.00	1015.2
298.15	50000.00	1017.5
318.15	100.00	969.9
318.15	10000.00	977.3
318.15	15000.00	980.4
318.15	20000.00	983.6
318.15	25000.00	986.9
318.15	30000.00	989.8
318.15	35000.00	992.9
318.15	40000.00	995.7
318.15	45000.00	998.6
318.15	50000.00	1001.5
348.15	100.00	941.3
348.15	10000.00	949.8
348.15	15000.00	953.5
348.15	20000.00	957.3
348.15	25000.00	961.1
348.15	30000.00	964.5
348.15	35000.00	967.9
348.15	40000.00	971.0
348.15	45000.00	974.5
348.15	50000.00	977.8
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[78.68; 302.13]	J/mol×K	[235.65; 1200.00]	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			-1.16340e+02
Coefficient B			-1.70410e+02
Coefficient C			5.92124e+00
Coefficient D			3.43680e-04
Coefficient E			-1.07670e-07
Temperature range, min.			235.65
Temperature range, max.			1200.00
Cp,gas	78.68	J/mol×K	235.65	Calculated Property
Cp,gas	135.63	J/mol×K	342.80	Calculated Property
Cp,gas	175.25	J/mol×K	449.95	Calculated Property
Cp,gas	205.29	J/mol×K	557.10	Calculated Property
Cp,gas	229.33	J/mol×K	664.25	Calculated Property
Cp,gas	249.20	J/mol×K	771.40	Calculated Property
Cp,gas	265.92	J/mol×K	878.55	Calculated Property
Cp,gas	280.10	J/mol×K	985.70	Calculated Property
Cp,gas	292.09	J/mol×K	1092.85	Calculated Property
Cp,gas	302.13	J/mol×K	1200.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[181.44; 249.23]	J/mol×K	[245.20; 484.20]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.28070e+02
Coefficient B			-7.76150e+01
Coefficient C			3.09424e+00
Coefficient D			5.96310e-03
Coefficient E			-4.36830e-06
Temperature range, min.			245.20
Temperature range, max.			484.20
Cp,liquid	181.44	J/mol×K	245.20	Calculated Property
Cp,liquid	188.81	J/mol×K	271.76	Calculated Property
Cp,liquid	196.39	J/mol×K	298.31	Calculated Property
Cp,liquid	204.13	J/mol×K	324.87	Calculated Property
Cp,liquid	211.96	J/mol×K	351.42	Calculated Property
Cp,liquid	219.79	J/mol×K	377.98	Calculated Property
Cp,liquid	227.53	J/mol×K	404.53	Calculated Property
Cp,liquid	235.09	J/mol×K	431.09	Calculated Property
Cp,liquid	242.36	J/mol×K	457.64	Calculated Property
Cp,liquid	249.23	J/mol×K	484.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0034305; 0.0001491]	Pa×s	[235.65; 542.00]	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			-1.68640e+01
Coefficient B			1.57260e+03
Coefficient C			8.28980e-01
Coefficient D			-2.28280e-07
Coefficient E			2.00000e+00
Temperature range, min.			235.65
Temperature range, max.			542.00
η	0.0034305	Pa×s	235.65	Calculated Property
η	0.0016460	Pa×s	269.69	Calculated Property
η	0.0009407	Pa×s	303.73	Calculated Property
η	0.0006067	Pa×s	337.77	Calculated Property
η	0.0004266	Pa×s	371.81	Calculated Property
η	0.0003198	Pa×s	405.84	Calculated Property
η	0.0002516	Pa×s	439.88	Calculated Property
η	0.0002056	Pa×s	473.92	Calculated Property
η	0.0001730	Pa×s	507.96	Calculated Property
η	0.0001491	Pa×s	542.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[50.46; 15.71]	kJ/mol	[235.65; 624.02]	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			6.17820e+01
Coefficient B			2.96540e-01
Coefficient C			8.16370e-01
Coefficient D			-1.37620e+00
Coefficient E			6.46840e-01
Critical temperature, Tc (K)			6.42150e+02
Temperature range, min.			235.65
Temperature range, max.			624.02
ΔvapH	50.46	kJ/mol	235.65	Calculated Property
ΔvapH	47.97	kJ/mol	278.80	Calculated Property
ΔvapH	45.44	kJ/mol	321.95	Calculated Property
ΔvapH	42.87	kJ/mol	365.11	Calculated Property
ΔvapH	40.20	kJ/mol	408.26	Calculated Property
ΔvapH	37.33	kJ/mol	451.41	Calculated Property
ΔvapH	34.09	kJ/mol	494.56	Calculated Property
ΔvapH	30.15	kJ/mol	537.72	Calculated Property
ΔvapH	24.85	kJ/mol	580.87	Calculated Property
ΔvapH	15.71	kJ/mol	624.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[2.46e-03; 4360.26]	kPa	[235.65; 642.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.10150e+02
Coefficient B			-9.31899e+03
Coefficient C			-1.41257e+01
Coefficient D			9.85051e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 645.6 K.
Temperature range, min.			235.65
Temperature range, max.			642.15
Pvap	2.46e-03	kPa	235.65	Calculated Property
Pvap	0.15	kPa	280.82	Calculated Property
Pvap	2.38	kPa	325.98	Calculated Property
Pvap	16.83	kPa	371.15	Calculated Property
Pvap	71.89	kPa	416.32	Calculated Property
Pvap	221.76	kPa	461.48	Calculated Property
Pvap	552.00	kPa	506.65	Calculated Property
Pvap	1192.40	kPa	551.82	Calculated Property
Pvap	2347.80	kPa	596.98	Calculated Property
Pvap	4360.26	kPa	642.15	Calculated Property
Pvap	[26.55; 133.41]	kPa	[383.03; 437.26]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42237e+01
Coefficient B			-3.43029e+03
Coefficient C			-6.96070e+01
Reference			Collerson, Counsell, et al., 1965
Temperature range, min.			383.03
Temperature range, max.			437.26
Pvap	26.55	kPa	383.03	Calculated Property
Pvap	32.64	kPa	389.06	Calculated Property
Pvap	39.82	kPa	395.08	Calculated Property
Pvap	48.22	kPa	401.11	Calculated Property
Pvap	58.01	kPa	407.13	Calculated Property
Pvap	69.33	kPa	413.16	Calculated Property
Pvap	82.35	kPa	419.18	Calculated Property
Pvap	97.24	kPa	425.21	Calculated Property
Pvap	114.20	kPa	431.23	Calculated Property
Pvap	133.41	kPa	437.26	Calculated Property
Pvap	[26.55; 133.41]	kPa	[383.03; 437.26]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42237e+01
Coefficient B			-3.43029e+03
Coefficient C			-6.96070e+01
Reference			Collerson, Counsell, et al., 1965, 2
Temperature range, min.			383.03
Temperature range, max.			437.26
Pvap	26.55	kPa	383.03	Calculated Property
Pvap	32.64	kPa	389.06	Calculated Property
Pvap	39.82	kPa	395.08	Calculated Property
Pvap	48.22	kPa	401.11	Calculated Property
Pvap	58.01	kPa	407.13	Calculated Property
Pvap	69.33	kPa	413.16	Calculated Property
Pvap	82.35	kPa	419.18	Calculated Property
Pvap	97.24	kPa	425.21	Calculated Property
Pvap	114.20	kPa	431.23	Calculated Property
Pvap	133.41	kPa	437.26	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1044.23; 427.28]	kg/m3	[235.65; 642.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.30190e+01
Coefficient B			2.44310e-01
Coefficient C			6.45610e+02
Coefficient D			2.62390e-01
Comment			Range stopped at Tc; ChemSep gives it to 645.6 K.
Temperature range, min.			235.65
Temperature range, max.			642.15
ρl	1044.23	kg/m3	235.65	Calculated Property
ρl	1005.56	kg/m3	280.82	Calculated Property
ρl	964.82	kg/m3	325.98	Calculated Property
ρl	921.52	kg/m3	371.15	Calculated Property
ρl	874.92	kg/m3	416.32	Calculated Property
ρl	823.90	kg/m3	461.48	Calculated Property
ρl	766.53	kg/m3	506.65	Calculated Property
ρl	698.94	kg/m3	551.82	Calculated Property
ρl	610.98	kg/m3	596.98	Calculated Property
ρl	427.28	kg/m3	642.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[235.65; 426.95]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			7.09973e-02
Coefficient B			-1.20400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			235.65
Temperature range, max.			426.95
γ	0.04	N/m	235.65	Calculated Property
γ	0.04	N/m	256.91	Calculated Property
γ	0.04	N/m	278.16	Calculated Property
γ	0.03	N/m	299.42	Calculated Property
γ	0.03	N/m	320.67	Calculated Property
γ	0.03	N/m	341.93	Calculated Property
γ	0.03	N/m	363.18	Calculated Property
γ	0.02	N/m	384.44	Calculated Property
γ	0.02	N/m	405.69	Calculated Property
γ	0.02	N/m	426.95	Calculated Property
γ	[0.04; 8.97e-04]	N/m	[235.65; 624.02]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.02800e-02
Coefficient B			7.61850e+01
Coefficient C			-3.35740e+00
Coefficient D			1.87900e-03
Coefficient E			-6.24330e-06
Temperature range, min.			235.65
Temperature range, max.			624.02
γ	0.04	N/m	235.65	Calculated Property
γ	0.04	N/m	278.80	Calculated Property
γ	0.03	N/m	321.95	Calculated Property
γ	0.03	N/m	365.11	Calculated Property
γ	0.02	N/m	408.26	Calculated Property
γ	0.02	N/m	451.41	Calculated Property
γ	0.01	N/m	494.56	Calculated Property
γ	0.01	N/m	537.72	Calculated Property
γ	0.00	N/m	580.87	Calculated Property
γ	8.97e-04	N/m	624.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[235.65; 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			5.53560e-04
Coefficient B			7.62400e-01
Coefficient C			3.42480e+02
Coefficient D			2.35670e+05
Temperature range, min.			235.65
Temperature range, max.			1000.00
λgas	0.01	W/m×K	235.65	Calculated Property
λgas	0.01	W/m×K	320.58	Calculated Property
λgas	0.02	W/m×K	405.51	Calculated Property
λgas	0.02	W/m×K	490.43	Calculated Property
λgas	0.03	W/m×K	575.36	Calculated Property
λgas	0.04	W/m×K	660.29	Calculated Property
λgas	0.05	W/m×K	745.22	Calculated Property
λgas	0.05	W/m×K	830.14	Calculated Property
λgas	0.06	W/m×K	915.07	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.10]	W/m×K	[192.50; 512.50]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-1.59590e-01
Coefficient B			2.11420e+01
Coefficient C			-1.13730e+00
Coefficient D			-2.37380e-06
Coefficient E			-9.75700e-07
Temperature range, min.			192.50
Temperature range, max.			512.50
λliquid	0.19	W/m×K	192.50	Calculated Property
λliquid	0.17	W/m×K	228.06	Calculated Property
λliquid	0.16	W/m×K	263.61	Calculated Property
λliquid	0.16	W/m×K	299.17	Calculated Property
λliquid	0.15	W/m×K	334.72	Calculated Property
λliquid	0.14	W/m×K	370.28	Calculated Property
λliquid	0.13	W/m×K	405.83	Calculated Property
λliquid	0.12	W/m×K	441.39	Calculated Property
λliquid	0.11	W/m×K	476.94	Calculated Property
λliquid	0.10	W/m×K	512.50	Calculated Property

Similar Compounds

Find more compounds similar to Anisole.

Mixtures

• Ethanol + Anisole
• 1-Propanol + Anisole
• 2-Propanol + Anisole
• 1-Butanol + Anisole
• Anisole + 1-Pentanol
• 1-Butanol, 3-methyl- + Anisole
• 1,2-Ethanediol + Anisole
• Anisole + 2,2',4,4',6,6'-Hexanitrobiphenyl
• Carbonic acid, dimethyl ester + Anisole + Water
• Anisole + Methyl Alcohol + Water
• Anisole + Methyl Alcohol
• Carbonic acid, dimethyl ester + Anisole
• Anisole + Water
• nitric acid + Anisole + Water
• Acetic acid, butyl ester + Anisole
• n-Hexane + Anisole
• Anisole + Heptane
• Octane + Anisole
• Anisole + Nonane
• Decane + Anisole

Find more mixtures with Anisole.

Sources

• 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.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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.
• Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
• (Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
• Ternary liquid-liquid equilibrium: Nitric acid - water - anisole/4-methyl anisole
• Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
• Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
• Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
• The solid-liquid equilitbrium, excess molar volume and refractive deviation properties of binary systems containing dimethyl carbonate, anisole and phenol
• Determination and correlation of solubility of 2,2',4,4',6,6 '-hexanitro-1,1'-biphenyl and 2,2',2" ,4,4',4" ,6,6',6" -Nonanitro-1,1 ':3',1"-terphenyl in six pure solvents
• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
• Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
• Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
• Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
• (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 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
• PVT properties for binary ionic liquids of 1-methyl-1-propylpiperidinium bis(trifluoromethylsulfonyl)imide with anisole or acetophenone at pressures up to 50 MPa
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• P-V-T properties of binary mixtures of the ionic liquid 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide with anisole or acetophenone at elevated pressures
• Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
• The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
• Isobaric (vapour + liquid) equilibria of binary systems containing butyl acetate for the separation of methoxy aromatic compounds (anisole and guaiacol) from biomass fast pyrolysis oil
• The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
• Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
• Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
• The fusion thermochemistry of self-associated aromatic compounds at 298.15 K studied by solution calorimetry
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• New method for determination of vaporization and sublimation enthalpy of aromatic compounds at 298.15 K using solution calorimetry technique and group-additivity scheme
• Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
• Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
• Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
• Dilute Vapor Absorption: A New Accurate Technique for Measurement of the Limiting Activity Coefficient of Water in Hydrophobic Solvents of Lower Volatility
• Isobaric Vapor-Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa
• Solubility Measurement, Modeling, and Thermodynamic Functions for para-Methoxyphenylacetic Acid in Pure and Mixed Organic and Aqueous Systems
• Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
• Liquid-Liquid Equilibrium for Ternary Systems of Water + 2,2,3,3-Tetrafluoro-1-propanol + Anisole/1-Octanol at 298.2, 308.2, and 318.2 K
• Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
• Experimental Determination and Modeling of Liquid-Liquid Equilibrium for Ternary Mixtures of Ethylene Glycol + 1,2-Butanediol + 3-Heptanone or Anisole
• Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
• Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
• Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
• 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
• Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
• Solute Partitioning Between 1-n-Butyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid and Supercritical CO2
• Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
• Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures
• Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
• Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Anisole
• Joback Method
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB

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