Chemical Properties of Benzene, ethoxy- (CAS 103-73-1)

InChI

InChI=1S/C8H10O/c1-2-9-8-6-4-3-5-7-8/h3-7H,2H2,1H3

InChI Key

DLRJIFUOBPOJNS-UHFFFAOYSA-N

Formula

C8H10O

SMILES

CCOc1ccccc1

Molecular Weight¹

122.16

CAS

103-73-1

Other Names

• Benzyl methyl ether
• Ether, ethyl phenyl-
• Ethoxybenzene (phenetol)
• Phenoxyethane
• Phenyl ethyl ether
• ethoxybenzene
• ethyl phenyl ether
• phenetole

• ω : Acentric Factor.
• 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).
• 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_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).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced 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	[0.4153; 0.4180]
ω	0.4153		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4179		ChemSep v8.3 pure component data Compiled value
ω	0.4180		KDB
ΔcH°liquid	[-4424.59; -4417.84]	kJ/mol
ΔcH°liquid	-4424.59	kJ/mol	NIST
ΔcH°liquid	-4417.84	kJ/mol	NIST
μ	[1.20; 1.41]	debye
μ	1.41	debye	ChemSep v8.3 pure component data Compiled value
μ	1.20	debye	KDB
ΔfG°	17.45	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-125.00; -101.60]	kJ/mol
ΔfH°gas	-101.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-101.60 ± 1.20	kJ/mol	NIST
ΔfH°gas	-125.00	kJ/mol	NIST
ΔfH°gas	-108.40	kJ/mol	NIST
ΔfH°liquid	[-159.40; -152.60]	kJ/mol
ΔfH°liquid	-152.60 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-159.40	kJ/mol	NIST
ΔfusH°	11.70	kJ/mol	Joback Calculated Property
ΔvapH°	[50.70; 51.04]	kJ/mol
ΔvapH°	51.04	kJ/mol	NIST
ΔvapH°	50.70	kJ/mol	NIST
ΔvapH°	51.04 ± 0.12	kJ/mol	NIST
ΔvapH°	51.00	kJ/mol	NIST
ΔvapH°	51.00 ± 0.10	kJ/mol	NIST
IE	[8.13; 8.60]	eV
IE	8.60	eV	NIST
IE	8.13 ± 0.02	eV	NIST
IE	8.36	eV	NIST
IE	8.41	eV	NIST
log10WS	[-2.33; -2.33]
log10WS	-2.33		Aq. Solubility Prediction
log10WS	-2.33		Estimated Solubility
logPoct/wat	2.085		Crippen Calculated Property
McVol	105.690	ml/mol	McGowan Calculated Property
Pc	[3400.00; 3434.92]	kPa
Pc	3400.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3424.78	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3420.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3420.00	kPa	KDB
Pc	3420.00 ± 81.06	kPa	NIST
Pc	3434.92 ± 101.32	kPa	NIST
Pc	3414.65 ± 101.32	kPa	NIST
Ptriple	1.78e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[953.00; 996.00]
Inp	978.50		NIST
Inp	976.30		NIST
Inp	981.30		NIST
Inp	971.60		NIST
Inp	973.30		NIST
Inp	980.50		NIST
Inp	978.10		NIST
Inp	980.00		NIST
Inp	995.00		NIST
Inp	995.00		NIST
Inp	984.00		NIST
Inp	995.00		NIST
Inp	Outlier 953.70		NIST
Inp	Outlier 953.00		NIST
Inp	996.00		NIST
Inp	988.80		NIST
Inp	991.10		NIST
Inp	992.40		NIST
Inp	970.80		NIST
Inp	988.80		NIST
Inp	991.10		NIST
Inp	992.40		NIST
Inp	980.00		NIST
Inp	980.00		NIST
Inp	978.50		NIST
Inp	980.50		NIST
Inp	984.00		NIST
Ip	[1437.00; 1442.00]
Ip	1437.00		NIST
Ip	1442.00		NIST
Tboil	[442.96; 445.15]	K
Tboil	443.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	442.96	K	KDB
Tboil	443.20	K	NIST
Tboil	443.15 ± 0.07	K	NIST
Tboil	443.10 ± 0.50	K	NIST
Tboil	442.96 ± 0.20	K	NIST
Tboil	443.60 ± 0.40	K	NIST
Tboil	443.60 ± 0.50	K	NIST
Tboil	443.50 ± 0.50	K	NIST
Tboil	443.60 ± 0.50	K	NIST
Tboil	443.50 ± 0.20	K	NIST
Tboil	443.30 ± 0.50	K	NIST
Tboil	443.50 ± 0.50	K	NIST
Tboil	Outlier 445.15 ± 1.50	K	NIST
Tc	[647.00; 647.15]	K
Tc	647.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	647.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	647.15	K	ChemSep v8.3 pure component data Compiled value
Tc	647.00	K	KDB
Tc	647.00 ± 2.00	K	NIST
Tc	647.15 ± 2.50	K	NIST
Tfus	[242.95; 243.68]	K
Tfus	243.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	243.63	K	ChemSep v8.3 pure component data Compiled value
Tfus	243.63	K	KDB
Tfus	243.32	K	Aq. Solubility Prediction
Tfus	243.63 ± 0.05	K	NIST
Tfus	243.68 ± 0.30	K	NIST
Tfus	243.48 ± 0.30	K	NIST
Tfus	242.95 ± 0.30	K	NIST
Ttriple	243.63	K	ChemSep v8.3 pure component data Compiled value
UQi	3.75		ChemSep v8.3 pure component data Compiled value
URi	4.84		ChemSep v8.3 pure component data Compiled value
Vc	[0.389; 0.390]	m3/kmol
Vc	0.389	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.390	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2480000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	228.50	J/mol×K	298.15	NIST
ΔvapH	[40.70; 44.50]	kJ/mol	[422.00; 427.00]
ΔvapH	44.50	kJ/mol	422.00	NIST
ΔvapH	40.70	kJ/mol	422.00	NIST
ΔvapH	44.00	kJ/mol	427.00	NIST
n0	[1.50020; 1.50580]		[298.15; 308.15]
n0	1.50580		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	1.50020		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
ρl	[942.50; 979.00]	kg/m3	[277.00; 318.15]
ρl	979.00	kg/m3	277.00	KDB
ρl	960.00	kg/m3	298.00	Densities, ultrasonic speeds and refractive indices of phenetole with N-methyl-2-pyrrolidone, N,N-dimethylformamide and tetrahydrofuran binary mixtures at different temperatures
ρl	960.20	kg/m3	298.15	Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
ρl	955.00	kg/m3	303.00	Densities, ultrasonic speeds and refractive indices of phenetole with N-methyl-2-pyrrolidone, N,N-dimethylformamide and tetrahydrofuran binary mixtures at different temperatures
ρl	951.00	kg/m3	308.00	Densities, ultrasonic speeds and refractive indices of phenetole with N-methyl-2-pyrrolidone, N,N-dimethylformamide and tetrahydrofuran binary mixtures at different temperatures
ρl	953.40	kg/m3	308.15	Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
ρl	942.50	kg/m3	318.15	Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	333.20	K	1.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[108.82; 390.34]	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			4.00000e+01
Coefficient B			-5.00000e+02
Coefficient C			6.19224e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	108.82	J/mol×K	255.00	Calculated Property
Cp,gas	177.15	J/mol×K	393.33	Calculated Property
Cp,gas	230.91	J/mol×K	531.67	Calculated Property
Cp,gas	271.82	J/mol×K	670.00	Calculated Property
Cp,gas	303.40	J/mol×K	808.33	Calculated Property
Cp,gas	328.32	J/mol×K	946.67	Calculated Property
Cp,gas	348.41	J/mol×K	1085.00	Calculated Property
Cp,gas	364.90	J/mol×K	1223.33	Calculated Property
Cp,gas	378.68	J/mol×K	1361.67	Calculated Property
Cp,gas	390.34	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[227.97; 287.97]	J/mol×K	[293.15; 485.36]	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			1.58400e+02
Coefficient B			1.92100e-01
Coefficient C			1.54210e-04
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			293.15
Temperature range, max.			485.36
Cp,liquid	227.97	J/mol×K	293.15	Calculated Property
Cp,liquid	234.07	J/mol×K	314.51	Calculated Property
Cp,liquid	240.31	J/mol×K	335.86	Calculated Property
Cp,liquid	246.70	J/mol×K	357.22	Calculated Property
Cp,liquid	253.23	J/mol×K	378.58	Calculated Property
Cp,liquid	259.89	J/mol×K	399.93	Calculated Property
Cp,liquid	266.70	J/mol×K	421.29	Calculated Property
Cp,liquid	273.65	J/mol×K	442.65	Calculated Property
Cp,liquid	280.74	J/mol×K	464.00	Calculated Property
Cp,liquid	287.97	J/mol×K	485.36	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0037742; 0.0002558]	Pa×s	[243.63; 445.15]	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			-2.74960e+01
Coefficient B			2.20740e+03
Coefficient C			2.33930e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			243.63
Temperature range, max.			445.15
η	0.0037742	Pa×s	243.63	Calculated Property
η	0.0021625	Pa×s	266.02	Calculated Property
η	0.0013718	Pa×s	288.41	Calculated Property
η	0.0009414	Pa×s	310.80	Calculated Property
η	0.0006873	Pa×s	333.19	Calculated Property
η	0.0005273	Pa×s	355.59	Calculated Property
η	0.0004211	Pa×s	377.98	Calculated Property
η	0.0003476	Pa×s	400.37	Calculated Property
η	0.0002948	Pa×s	422.76	Calculated Property
η	0.0002558	Pa×s	445.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[53.53; 0.00]	kJ/mol	[243.63; 647.15]	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			6.43370e+01
Coefficient B			3.89350e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.47150e+02
Temperature range, min.			243.63
Temperature range, max.			647.15
ΔvapH	53.53	kJ/mol	243.63	Calculated Property
ΔvapH	51.13	kJ/mol	288.47	Calculated Property
ΔvapH	48.54	kJ/mol	333.30	Calculated Property
ΔvapH	45.71	kJ/mol	378.14	Calculated Property
ΔvapH	42.58	kJ/mol	422.97	Calculated Property
ΔvapH	39.04	kJ/mol	467.81	Calculated Property
ΔvapH	34.90	kJ/mol	512.64	Calculated Property
ΔvapH	29.80	kJ/mol	557.48	Calculated Property
ΔvapH	22.75	kJ/mol	602.31	Calculated Property
ΔvapH	0.00	kJ/mol	647.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[327.97; 471.68]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47771e+01
Coefficient B			-3.92315e+03
Coefficient C			-5.72150e+01
Temperature range, min.			327.97
Temperature range, max.			471.68
Pvap	1.33	kPa	327.97	Calculated Property
Pvap	2.99	kPa	343.94	Calculated Property
Pvap	6.15	kPa	359.91	Calculated Property
Pvap	11.77	kPa	375.87	Calculated Property
Pvap	21.18	kPa	391.84	Calculated Property
Pvap	36.13	kPa	407.81	Calculated Property
Pvap	58.82	kPa	423.78	Calculated Property
Pvap	91.95	kPa	439.74	Calculated Property
Pvap	138.69	kPa	455.71	Calculated Property
Pvap	202.65	kPa	471.68	Calculated Property
Pvap	[1.78e-03; 3446.27]	kPa	[243.63; 647.15]	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			7.12632e+01
Coefficient B			-8.43140e+03
Coefficient C			-7.82260e+00
Coefficient D			7.38810e-18
Coefficient E			6.00000e+00
Temperature range, min.			243.63
Temperature range, max.			647.15
Pvap	1.78e-03	kPa	243.63	Calculated Property
Pvap	0.10	kPa	288.47	Calculated Property
Pvap	1.71	kPa	333.30	Calculated Property
Pvap	12.92	kPa	378.14	Calculated Property
Pvap	58.33	kPa	422.97	Calculated Property
Pvap	185.61	kPa	467.81	Calculated Property
Pvap	464.37	kPa	512.64	Calculated Property
Pvap	987.56	kPa	557.48	Calculated Property
Pvap	1894.91	kPa	602.31	Calculated Property
Pvap	3446.27	kPa	647.15	Calculated Property
Pvap	[1.83e-03; 3360.08]	kPa	[243.63; 647.15]	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			9.30608e+01
Coefficient B			-9.14632e+03
Coefficient C			-1.13117e+01
Coefficient D			5.75060e-06
Coefficient E			0.00000e+00
Temperature range, min.			243.63
Temperature range, max.			647.15
Pvap	1.83e-03	kPa	243.63	Calculated Property
Pvap	0.11	kPa	288.47	Calculated Property
Pvap	1.73	kPa	333.30	Calculated Property
Pvap	12.90	kPa	378.14	Calculated Property
Pvap	57.98	kPa	422.97	Calculated Property
Pvap	185.40	kPa	467.81	Calculated Property
Pvap	468.71	kPa	512.64	Calculated Property
Pvap	1004.64	kPa	557.48	Calculated Property
Pvap	1915.39	kPa	602.31	Calculated Property
Pvap	3360.08	kPa	647.15	Calculated Property
Pvap	[20.44; 133.47]	kPa	[390.58; 453.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41487e+01
Coefficient B			-3.47061e+03
Coefficient C			-7.87930e+01
Reference			Collerson, Counsell, et al., 1965, 2
Temperature range, min.			390.58
Temperature range, max.			453.80
Pvap	20.44	kPa	390.58	Calculated Property
Pvap	26.12	kPa	397.60	Calculated Property
Pvap	33.03	kPa	404.63	Calculated Property
Pvap	41.35	kPa	411.65	Calculated Property
Pvap	51.29	kPa	418.68	Calculated Property
Pvap	63.07	kPa	425.70	Calculated Property
Pvap	76.93	kPa	432.73	Calculated Property
Pvap	93.10	kPa	439.75	Calculated Property
Pvap	111.86	kPa	446.78	Calculated Property
Pvap	133.47	kPa	453.80	Calculated Property
Pvap	[20.44; 133.47]	kPa	[390.58; 453.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41487e+01
Coefficient B			-3.47061e+03
Coefficient C			-7.87930e+01
Reference			Collerson, Counsell, et al., 1965
Temperature range, min.			390.58
Temperature range, max.			453.80
Pvap	20.44	kPa	390.58	Calculated Property
Pvap	26.12	kPa	397.60	Calculated Property
Pvap	33.03	kPa	404.63	Calculated Property
Pvap	41.35	kPa	411.65	Calculated Property
Pvap	51.29	kPa	418.68	Calculated Property
Pvap	63.07	kPa	425.70	Calculated Property
Pvap	76.93	kPa	432.73	Calculated Property
Pvap	93.10	kPa	439.75	Calculated Property
Pvap	111.86	kPa	446.78	Calculated Property
Pvap	133.47	kPa	453.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1008.67; 313.25]	kg/m3	[243.63; 647.15]	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			8.16923e+01
Coefficient B			2.60790e-01
Coefficient C			6.47150e+02
Coefficient D			2.94700e-01
Temperature range, min.			243.63
Temperature range, max.			647.15
ρl	1008.67	kg/m3	243.63	Calculated Property
ρl	969.22	kg/m3	288.47	Calculated Property
ρl	927.88	kg/m3	333.30	Calculated Property
ρl	884.20	kg/m3	378.14	Calculated Property
ρl	837.48	kg/m3	422.97	Calculated Property
ρl	786.67	kg/m3	467.81	Calculated Property
ρl	729.94	kg/m3	512.64	Calculated Property
ρl	663.60	kg/m3	557.48	Calculated Property
ρl	577.66	kg/m3	602.31	Calculated Property
ρl	313.25	kg/m3	647.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[243.65; 443.15]	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			6.53258e-02
Coefficient B			-1.10400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			243.65
Temperature range, max.			443.15
γ	0.04	N/m	243.65	Calculated Property
γ	0.04	N/m	265.82	Calculated Property
γ	0.03	N/m	287.98	Calculated Property
γ	0.03	N/m	310.15	Calculated Property
γ	0.03	N/m	332.32	Calculated Property
γ	0.03	N/m	354.48	Calculated Property
γ	0.02	N/m	376.65	Calculated Property
γ	0.02	N/m	398.82	Calculated Property
γ	0.02	N/m	420.98	Calculated Property
γ	0.02	N/m	443.15	Calculated Property
γ	[0.04; 0.00]	N/m	[243.63; 647.15]	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			6.78790e-02
Coefficient B			1.19990e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.47150e+02
Temperature range, min.			243.63
Temperature range, max.			647.15
γ	0.04	N/m	243.63	Calculated Property
γ	0.03	N/m	288.47	Calculated Property
γ	0.03	N/m	333.30	Calculated Property
γ	0.02	N/m	378.14	Calculated Property
γ	0.02	N/m	422.97	Calculated Property
γ	0.01	N/m	467.81	Calculated Property
γ	0.01	N/m	512.64	Calculated Property
γ	0.01	N/m	557.48	Calculated Property
γ	0.00	N/m	602.31	Calculated Property
γ	0.00	N/m	647.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.07]	W/m×K	[443.15; 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			7.12180e-04
Coefficient B			7.27200e-01
Coefficient C			3.89210e+02
Coefficient D			2.39620e+05
Temperature range, min.			443.15
Temperature range, max.			1000.00
λgas	0.02	W/m×K	443.15	Calculated Property
λgas	0.02	W/m×K	505.02	Calculated Property
λgas	0.03	W/m×K	566.89	Calculated Property
λgas	0.03	W/m×K	628.77	Calculated Property
λgas	0.04	W/m×K	690.64	Calculated Property
λgas	0.05	W/m×K	752.51	Calculated Property
λgas	0.05	W/m×K	814.38	Calculated Property
λgas	0.06	W/m×K	876.26	Calculated Property
λgas	0.06	W/m×K	938.13	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.12]	W/m×K	[243.63; 443.15]	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			1.87560e-01
Coefficient B			-1.60400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			243.63
Temperature range, max.			443.15
λliquid	0.15	W/m×K	243.63	Calculated Property
λliquid	0.14	W/m×K	265.80	Calculated Property
λliquid	0.14	W/m×K	287.97	Calculated Property
λliquid	0.14	W/m×K	310.14	Calculated Property
λliquid	0.13	W/m×K	332.31	Calculated Property
λliquid	0.13	W/m×K	354.47	Calculated Property
λliquid	0.13	W/m×K	376.64	Calculated Property
λliquid	0.12	W/m×K	398.81	Calculated Property
λliquid	0.12	W/m×K	420.98	Calculated Property
λliquid	0.12	W/m×K	443.15	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, ethoxy-.

Mixtures

• Benzene, ethoxy- + 2-Pyrrolidinone, 1-methyl-
• Benzene, ethoxy- + Formamide, N,N-dimethyl-
• Benzene, ethoxy- + Tetrahydrofuran
• Benzene, ethoxy- + Benzyl alcohol
• Benzene, ethoxy- + Phenylethyl Alcohol
• 3-Phenylpropanol + Benzene, ethoxy-

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.
• 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.
• Crippen Method
• Solubility predictions of acetanilide derivatives in water: Combining thermochemistry and thermodynamic modeling
• Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
• Densities, ultrasonic speeds and refractive indices of phenetole with N-methyl-2-pyrrolidone, N,N-dimethylformamide and tetrahydrofuran binary mixtures at different temperatures
• Sublimation enthalpies of 9 substituted acetanilides at 298 K estimated by solution calorimetry approach
• Dilute Vapor Absorption: A New Accurate Technique for Measurement of the Limiting Activity Coefficient of Water in Hydrophobic Solvents of Lower Volatility
• 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
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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