Chemical Properties of Ethanol, 2-phenoxy- (CAS 122-99-6)

InChI

InChI=1S/C8H10O2/c9-6-7-10-8-4-2-1-3-5-8/h1-5,9H,6-7H2

InChI Key

QCDWFXQBSFUVSP-UHFFFAOYSA-N

Formula

C8H10O2

SMILES

OCCOc1ccccc1

Molecular Weight¹

138.16

CAS

122-99-6

Other Names

• .beta.-phenoxyethyl alcohol
• 1-Hydroxy-2-phenoxyethane
• 2-Fenoxyethanol
• 2-Hydroxyethyl phenyl ether
• 2-Phenoxyethanol
• 2-Phenoxyethanol (rose ether)
• 2-Phenoxyethyl alcohol
• Arosol
• Dowanol EP
• Dowanol eph
• Emeressence 1160
• Emery 6705
• Ethylene glycol monophenyl ether
• Ethylene glycol phenyl ether
• Fenyl-cellosolve
• Fenylcelosolv
• Glycol monophenyl ether
• NSC 1864
• Phenoxethol
• Phenoxetol
• Phenoxyethanol
• Phenoxyethyl alcohol
• Phenoxyl ethanol
• Phenoxytol
• Phenyl cellosolve
• Phenylmonoglycol ether
• Rose ether
• «beta»-Hydroxyethyl phenyl ether
• «beta»-Phenoxyethanol
• «beta»-Phenoxyethyl alcohol
• «beta»-Hydroxyethyl phenyl ether
• «beta»-Phenoxyethanol
• «beta»-Phenoxyethyl alcohol

• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• 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_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).
• 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_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔfG°	-112.93	kJ/mol	Joback Calculated Property
ΔfH°gas	-256.37	kJ/mol	Joback Calculated Property
ΔfusH°	15.79	kJ/mol	Joback Calculated Property
ΔvapH°	54.77	kJ/mol	Joback Calculated Property
log10WS	[-0.70; -0.70]
log10WS	-0.70		Aq. Sol...
log10WS	-0.70		Estimat...
logPoct/wat	1.058		Crippen Calculated Property
McVol	111.560	ml/mol	McGowan Calculated Property
Pc	4005.77	kPa	Joback Calculated Property
Inp	[1185.00; 1245.30]
Inp	1210.00		NIST
Inp	1214.00		NIST
Inp	1191.60		NIST
Inp	1186.00		NIST
Inp	1221.00		NIST
Inp	1223.00		NIST
Inp	1226.00		NIST
Inp	1245.30		NIST
Inp	1229.00		NIST
Inp	1221.00		NIST
Inp	1194.00		NIST
Inp	1220.00		NIST
Inp	1213.00		NIST
Inp	1226.00		NIST
Inp	1226.00		NIST
Inp	1189.00		NIST
Inp	1185.00		NIST
Inp	1221.00		NIST
Inp	1191.60		NIST
Inp	1220.00		NIST
Inp	1185.00		NIST
I	[2080.00; 2144.00]
I	2103.00		NIST
I	2087.00		NIST
I	2144.00		NIST
I	2126.00		NIST
I	2142.00		NIST
I	2107.00		NIST
I	2080.00		NIST
I	2115.00		NIST
I	2100.00		NIST
I	2139.00		NIST
I	2115.00		NIST
I	2103.00		NIST
Tboil	[510.20; 518.20]	K
Tboil	510.20	K	NIST
Tboil	518.20	K	NIST
Tc	719.69	K	Joback Calculated Property
Tfus	285.90	K	Aq. Sol...
Vc	0.412	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[245.88; 300.95]	J/mol×K	[523.72; 719.69]
Cp,gas	245.88	J/mol×K	523.72	Joback Calculated Property
Cp,gas	256.37	J/mol×K	556.38	Joback Calculated Property
Cp,gas	266.32	J/mol×K	589.04	Joback Calculated Property
Cp,gas	275.73	J/mol×K	621.70	Joback Calculated Property
Cp,gas	284.64	J/mol×K	654.37	Joback Calculated Property
Cp,gas	293.04	J/mol×K	687.03	Joback Calculated Property
Cp,gas	300.95	J/mol×K	719.69	Joback Calculated Property
Cp,liquid	294.63	J/mol×K	298.15	NIST
η	[0.0001115; 0.0104901]	Pa×s	[289.39; 523.72]
η	0.0104901	Pa×s	289.39	Joback Calculated Property
η	0.0031358	Pa×s	328.44	Joback Calculated Property
η	0.0012117	Pa×s	367.50	Joback Calculated Property
η	0.0005620	Pa×s	406.56	Joback Calculated Property
η	0.0002983	Pa×s	445.61	Joback Calculated Property
η	0.0001753	Pa×s	484.67	Joback Calculated Property
η	0.0001115	Pa×s	523.72	Joback Calculated Property
ΔvapH	66.00	kJ/mol	435.00	NIST
ρl	[1081.00; 1107.00]	kg/m3	[293.15; 323.15]
ρl	1107.00	kg/m3	293.15	Density...
ρl	1103.00	kg/m3	298.15	Density...
ρl	1103.41	kg/m3	298.15	THERMOD...
ρl	1099.00	kg/m3	303.15	Density...
ρl	1090.00	kg/m3	313.15	Density...
ρl	1081.00	kg/m3	323.15	Density...

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[394.33; 547.68]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.55600e+01
Coefficient B			-4.77760e+03
Coefficient C			-8.15080e+01
Temperature range, min.			394.33
Temperature range, max.			547.68
Pvap	1.33	kPa	394.33	Calculated Property
Pvap	2.93	kPa	411.37	Calculated Property
Pvap	5.98	kPa	428.41	Calculated Property
Pvap	11.39	kPa	445.45	Calculated Property
Pvap	20.48	kPa	462.49	Calculated Property
Pvap	35.04	kPa	479.52	Calculated Property
Pvap	57.36	kPa	496.56	Calculated Property
Pvap	90.30	kPa	513.60	Calculated Property
Pvap	137.37	kPa	530.64	Calculated Property
Pvap	202.65	kPa	547.68	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol, 2-phenoxy-.

Mixtures

• 1-Propanol + Ethanol, 2-phenoxy-
• Isopropyl Alcohol + Ethanol, 2-phenoxy-
• Ethanol, 2-phenoxy- + 1-Butanol
• Ethanol, 2-phenoxy- + Heptane
• Ethanol, 2-phenoxy- + Octane
• Ethanol, 2-phenoxy- + Cyclohexane
• Ethanol, 2-phenoxy- + Cyclohexane, methyl-
• Cyclohexane, ethyl- + Ethanol, 2-phenoxy-

Sources

• Crippen Method
• Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
• THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
• Joback Method
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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