Ethanol, 2-(2-methoxyethoxy)- (CAS 111-77-3)

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Physical Properties

Property	Value	Unit	Source
ω	0.5141		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Δ_cH°_liquid	-3010.00	kJ/mol	NIST
T_flash,cc	366.15	K	NCMS SOLV-DB
Δ_fH°_gas	-567.95	kJ/mol	Relay (1.0) Calculated Property
Δ_fH°_liquid	-670.30	kJ/mol	NIST
Δ_fusH°	15.17	kJ/mol	Joback Calculated Property
Δ_vapH°	46.57	kJ/mol	NCMS SOLV-DB
IE	9.96	eV	Relay (1.0) Calculated Property
log₁₀WS	0.99		Relay (1.0) Calculated Property
logP_oct/wat	-1.180		NCMS SOLV-DB
McVol	98.920	ml/mol	McGowan Calculated Property
NFPA Fire	1		NCMS SOLV-DB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
P_c	[3670.00; 3670.00]	kPa
P_c	3670.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
P_c	3670.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
P_c	3670.00 ± 150.00	kPa	NIST
I_np	[907.00; 947.00]
I_np	907.00		NIST
I_np	932.00		NIST
I_np	937.80		NIST
I_np	908.00		NIST
I_np	947.00		NIST
I_np	920.00		NIST
I_np	924.00		NIST
I_np	907.00		NIST
I_np	920.00		NIST
I_np	937.80		NIST
I_p	[1553.00; 1620.00]
I_p	1553.00		NIST
I_p	1620.00		NIST
I_p	1589.00		NIST
I_p	1576.00		NIST
I_p	1576.00		NIST
T_boil	[466.10; 502.40]	K
T_boil	466.15	K	NCMS SOLV-DB
T_boil	466.20	K	NIST
T_boil	466.10 ± 0.70	K	NIST
T_boil	502.40 ± 2.50	K	NIST
T_boil	471.00 ± 3.00	K	NIST
T_c	[672.00; 672.00]	K
T_c	672.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
T_c	672.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
T_c	672.00 ± 2.00	K	NIST
T_fus	[189.15; 203.15]	K
T_fus	203.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
T_fus	189.15	K	NCMS SOLV-DB
V_c	0.371	m³/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[261.90; 280.10]	J/mol×K	[275.15; 339.15]

C_p,liquid	261.90	J/mol×K	275.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	262.30	J/mol×K	277.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	262.70	J/mol×K	279.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	263.20	J/mol×K	281.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	263.60	J/mol×K	283.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	264.10	J/mol×K	285.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	264.60	J/mol×K	287.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	265.10	J/mol×K	289.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	265.60	J/mol×K	291.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	266.10	J/mol×K	293.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	266.60	J/mol×K	295.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	267.10	J/mol×K	297.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	267.40	J/mol×K	298.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	267.60	J/mol×K	299.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	268.20	J/mol×K	301.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	268.70	J/mol×K	303.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	269.30	J/mol×K	305.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	269.80	J/mol×K	307.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	270.40	J/mol×K	309.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	271.00	J/mol×K	311.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	271.60	J/mol×K	313.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	272.20	J/mol×K	315.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	272.80	J/mol×K	317.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	273.40	J/mol×K	319.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	274.00	J/mol×K	321.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	274.70	J/mol×K	323.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	275.30	J/mol×K	325.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	276.00	J/mol×K	327.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	276.60	J/mol×K	329.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	277.30	J/mol×K	331.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	278.00	J/mol×K	333.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	278.70	J/mol×K	335.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	279.40	J/mol×K	337.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
C_p,liquid	280.10	J/mol×K	339.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
η	0.0034800	Pa×s	298.15	NCMS SOLV-DB
Δ_vapH	51.90	kJ/mol	425.50	NIST
P_vap	0.02	kPa	298.15	NCMS SOLV-DB
n₀	[1.42400; 1.42500]		[298.15; 298.15]
n₀	1.42420		298.15	Physical and excess properties of a room temperature ionic liquid (1-methyl-3-octylimidazolium tetrafluoroborate) with n-alkoxyethanols (C1Em, m = 1 to 3) at T = (298.15 to 318.15) K
n₀	1.42500		298.15	Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
n₀	1.42450		298.15	Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
n₀	1.42400		298.15	NCMS SOLV-DB
ρ_l	[948.50; 1028.60]	kg/m³	[283.15; 373.15]

ρ_l	1028.60	kg/m³	283.15	Thermophysical properties of glycols and glymes
ρ_l	1024.20	kg/m³	288.15	Thermophysical properties of glycols and glymes
ρ_l	1025.30	kg/m³	288.15	Thermophysical properties of glycols and glymes
ρ_l	1021.00	kg/m³	293.15	Thermophysical properties of glycols and glymes
ρ_l	1020.80	kg/m³	293.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρ_l	1019.80	kg/m³	293.15	Thermophysical properties of glycols and glymes
ρ_l	1016.40	kg/m³	298.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρ_l	1016.30	kg/m³	298.15	Thermophysical properties of glycols and glymes
ρ_l	1015.60	kg/m³	298.15	Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
ρ_l	1015.40	kg/m³	298.15	Thermophysical properties of glycols and glymes
ρ_l	1016.43	kg/m³	298.15	Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
ρ_l	1011.90	kg/m³	303.15	Thermophysical properties of glycols and glymes
ρ_l	1011.83	kg/m³	303.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρ_l	1011.00	kg/m³	303.15	Thermophysical properties of glycols and glymes
ρ_l	1007.69	kg/m³	308.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρ_l	1006.60	kg/m³	308.15	Thermophysical properties of glycols and glymes
ρ_l	1007.40	kg/m³	308.15	Thermophysical properties of glycols and glymes
ρ_l	1003.00	kg/m³	313.15	Thermophysical properties of glycols and glymes
ρ_l	1002.10	kg/m³	313.15	Thermophysical properties of glycols and glymes
ρ_l	1003.22	kg/m³	313.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρ_l	998.80	kg/m³	318.15	Thermophysical properties of glycols and glymes
ρ_l	993.20	kg/m³	323.15	Thermophysical properties of glycols and glymes
ρ_l	994.30	kg/m³	323.15	Thermophysical properties of glycols and glymes
ρ_l	989.80	kg/m³	328.15	Thermophysical properties of glycols and glymes
ρ_l	985.30	kg/m³	333.15	Thermophysical properties of glycols and glymes
ρ_l	984.10	kg/m³	333.15	Thermophysical properties of glycols and glymes
ρ_l	981.00	kg/m³	338.15	Thermophysical properties of glycols and glymes
ρ_l	976.50	kg/m³	343.15	Thermophysical properties of glycols and glymes
ρ_l	975.00	kg/m³	343.15	Thermophysical properties of glycols and glymes
ρ_l	971.80	kg/m³	348.15	Thermophysical properties of glycols and glymes
ρ_l	967.20	kg/m³	353.15	Thermophysical properties of glycols and glymes
ρ_l	962.50	kg/m³	358.15	Thermophysical properties of glycols and glymes
ρ_l	957.90	kg/m³	363.15	Thermophysical properties of glycols and glymes
ρ_l	953.10	kg/m³	368.15	Thermophysical properties of glycols and glymes
ρ_l	948.50	kg/m³	373.15	Thermophysical properties of glycols and glymes
c_sound,fluid	[1349.00; 1451.00]	m/s	[288.15; 318.15]

c_sound,fluid	1451.00	m/s	288.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
c_sound,fluid	1432.37	m/s	293.15	Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems
c_sound,fluid	1434.00	m/s	293.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
c_sound,fluid	1432.37	m/s	293.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
c_sound,fluid	1416.00	m/s	298.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
c_sound,fluid	1415.21	m/s	298.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
c_sound,fluid	1415.21	m/s	298.15	Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems
c_sound,fluid	1397.93	m/s	303.15	Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems
c_sound,fluid	1399.00	m/s	303.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
c_sound,fluid	1397.93	m/s	303.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
c_sound,fluid	1382.00	m/s	308.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
c_sound,fluid	1366.00	m/s	313.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
c_sound,fluid	1349.00	m/s	318.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
γ	[0.03; 0.03]	N/m	[298.15; 318.15]
γ	0.03	N/m	298.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	308.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
γ	0.03	N/m	318.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1028.5
283.15	1000.00	1029.0
283.15	2500.00	1029.8
283.15	5000.00	1031.2
283.15	7500.00	1032.5
283.15	10000.00	1033.9
283.15	15000.00	1036.4
283.15	20000.00	1039.0
283.15	25000.00	1041.4
293.15	100.00	1019.5
293.15	1000.00	1020.0
293.15	2500.00	1020.9
293.15	5000.00	1022.3
293.15	7500.00	1023.7
293.15	10000.00	1025.2
293.15	15000.00	1027.9
293.15	20000.00	1030.5
293.15	25000.00	1033.1
303.15	100.00	1010.8
303.15	1000.00	1011.3
303.15	2500.00	1012.2
303.15	5000.00	1013.6
303.15	7500.00	1015.0
303.15	10000.00	1016.4
303.15	15000.00	1019.3
303.15	20000.00	1022.1
303.15	25000.00	1024.8
313.15	100.00	1002.0
313.15	1000.00	1002.6
313.15	2500.00	1003.5
313.15	5000.00	1005.1
313.15	7500.00	1006.7
313.15	10000.00	1008.2
313.15	15000.00	1011.2
313.15	20000.00	1014.1
313.15	25000.00	1016.9
323.15	100.00	993.2
323.15	1000.00	993.9
323.15	2500.00	994.9
323.15	5000.00	996.6
323.15	7500.00	998.3
323.15	10000.00	1000.0
323.15	15000.00	1003.2
323.15	20000.00	1006.2
323.15	25000.00	1009.2
333.15	100.00	983.9
333.15	1000.00	984.6
333.15	2500.00	985.6
333.15	5000.00	987.4
333.15	7500.00	989.1
333.15	10000.00	990.8
333.15	15000.00	994.1
333.15	20000.00	997.2
333.15	25000.00	1000.2
343.15	100.00	975.2
343.15	1000.00	975.8
343.15	2500.00	977.0
343.15	5000.00	978.8
343.15	7500.00	980.6
343.15	10000.00	982.4
343.15	15000.00	985.9
343.15	20000.00	989.2
343.15	25000.00	992.4
353.15	100.00	965.7
353.15	1000.00	966.4
353.15	2500.00	967.6
353.15	5000.00	969.5
353.15	7500.00	971.4
353.15	10000.00	973.3
353.15	15000.00	976.9
353.15	20000.00	980.4
353.15	25000.00	983.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[154.86; 332.95]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is C_p,gas in J/mol×K, T in K
Coefficient A			5.46340e+01
Coefficient B			3.86420e-01
Coefficient C			-5.66000e-05
Coefficient D			-5.15000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00

C_p,gas	154.86	J/mol×K	273.00	Calculated Property
C_p,gas	181.98	J/mol×K	353.78	Calculated Property
C_p,gas	207.64	J/mol×K	434.56	Calculated Property
C_p,gas	231.69	J/mol×K	515.33	Calculated Property
C_p,gas	253.96	J/mol×K	596.11	Calculated Property
C_p,gas	274.29	J/mol×K	676.89	Calculated Property
C_p,gas	292.52	J/mol×K	757.67	Calculated Property
C_p,gas	308.48	J/mol×K	838.44	Calculated Property
C_p,gas	322.01	J/mol×K	919.22	Calculated Property
C_p,gas	332.95	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.66]	kPa	[357.72; 491.20]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.78402e+01
Coefficient B			-5.84302e+03
Coefficient C			-2.48290e+01
Temperature range, min.			357.72
Temperature range, max.			491.20

P_vap	1.33	kPa	357.72	Calculated Property
P_vap	2.82	kPa	372.55	Calculated Property
P_vap	5.61	kPa	387.38	Calculated Property
P_vap	10.56	kPa	402.21	Calculated Property
P_vap	18.97	kPa	417.04	Calculated Property
P_vap	32.64	kPa	431.88	Calculated Property
P_vap	54.06	kPa	446.71	Calculated Property
P_vap	86.53	kPa	461.54	Calculated Property
P_vap	134.29	kPa	476.37	Calculated Property
P_vap	202.66	kPa	491.20	Calculated Property
P_vap	[6.25; 99.30]	kPa	[385.50; 466.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.57006e+01
Coefficient B			-4.48125e+03
Coefficient C			-6.23740e+01
Reference			Dykyj, Seprakova, et al., 1957, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			385.50
Temperature range, max.			466.00

P_vap	6.25	kPa	385.50	Calculated Property
P_vap	9.08	kPa	394.44	Calculated Property
P_vap	12.93	kPa	403.39	Calculated Property
P_vap	18.09	kPa	412.33	Calculated Property
P_vap	24.89	kPa	421.28	Calculated Property
P_vap	33.73	kPa	430.22	Calculated Property
P_vap	45.04	kPa	439.17	Calculated Property
P_vap	59.34	kPa	448.11	Calculated Property
P_vap	77.21	kPa	457.06	Calculated Property
P_vap	99.30	kPa	466.00	Calculated Property
P_vap	[6.25; 99.30]	kPa	[385.50; 466.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.57006e+01
Coefficient B			-4.48125e+03
Coefficient C			-6.23740e+01
Reference			Dykyj, Seprakova, et al., 1957
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			385.50
Temperature range, max.			466.00

P_vap	6.25	kPa	385.50	Calculated Property
P_vap	9.08	kPa	394.44	Calculated Property
P_vap	12.93	kPa	403.39	Calculated Property
P_vap	18.09	kPa	412.33	Calculated Property
P_vap	24.89	kPa	421.28	Calculated Property
P_vap	33.73	kPa	430.22	Calculated Property
P_vap	45.04	kPa	439.17	Calculated Property
P_vap	59.34	kPa	448.11	Calculated Property
P_vap	77.21	kPa	457.06	Calculated Property
P_vap	99.30	kPa	466.00	Calculated Property

Similar Compounds

2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.

2-[2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.

Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-.

2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.

2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.

2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.

2-[2-[2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Hydroxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.

3,6,9,12,15,18,21,24,27,30-decaoxadotriacontane-1,32-diol.

3,6,9,12,15,18,21,24,27-nonaoxanonacosane-1,29-diol.

Find more compounds similar to Ethanol, 2-(2-methoxyethoxy)-.

Mixtures

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.
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.
Cheméo Relay (1.0)
Crippen Method
Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
Partial molar volumes of organic solutes in water. XVIII: Selected polyethers(aq) and 3,6-dioxa-1-heptanol(aq) at T = (298 to 573) K and at pressures up to 30 MPa
Physical and excess properties of a room temperature ionic liquid (1-methyl-3-octylimidazolium tetrafluoroborate) with n-alkoxyethanols (C1Em, m = 1 to 3) at T = (298.15 to 318.15) K
Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
Thermophysical properties of ionic liquid {1-butyl-3-methylimidazolium bromide [bmim][Br] in alkoxyalkanols + water} mixtures at different temperatures
Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Thermophysical properties of glycols and glymes
Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
Liquid Density Measurements of Diethylene Glycol Monoalkyl Ethers as a Function of Temperature and Pressure
Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems
Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
Joback Method
McGowan Method
NIST Webbook
NCMS SOLV-DB
The Yaws Handbook of Vapor Pressure

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Chemical Properties of Ethanol, 2-(2-methoxyethoxy)- (CAS 111-77-3)