Chemical Properties of Ethanol, 2,2'-oxybis- (CAS 111-46-6)

InChI

InChI=1S/C4H10O3/c5-1-3-7-4-2-6/h5-6H,1-4H2

InChI Key

MTHSVFCYNBDYFN-UHFFFAOYSA-N

Formula

C4H10O3

SMILES

OCCOCCO

Molecular Weight¹

106.12

CAS

111-46-6

Other Names

• 1,1'-oxybis[1-methoxy]methane
• 1,5-Dihydroxy-3-oxapentane
• 2,2'-Dihydroxyethyl ether
• 2,2'-OXYBIS ETHANOL
• 2,2'-Oxybis[Ethanol]
• 2,2'-Oxydiethanol
• 2,2'-Oxyethanol
• 2,2'-oxybis(ethan-1-ol)
• 2,2'-oxybis-ethanol
• 2,2-Di(hydroxyethyl) ether
• 2,4,6-trioxaheptane
• 2-(2-Hydroxyethoxy)ethanol
• 2-Hydroxyethyl ether
• 3-Oxa-1,5-pentanediol
• 3-Oxapentamethylene-1,5-diol
• 3-Oxapentane-1,5-diol
• 3-oxapentan-1,5-diol
• BETA,BETA'-DIHYDROXYDIETHYL ETHER
• Bis(2-hydroxyethyl) ether
• Bis(«beta»-hydroxyethyl) ether
• Bis(«beta»-hydroxyethyl) ether
• Brecolane NDG
• Carbitol
• D.E.H. 20
• D.E.H. 52
• DEG
• Deactivator E
• Deactivator H
• Dicol
• Diethylene glycol
• Diethylenglykol
• Digenos
• Diglycol
• Digol
• Dihydroxydiethyl ether
• Dissolvant APV
• ETHYLENE DIGLYCOL
• Ethanol, 2,2'-oxydi-
• Glycol ether
• Glycol hydroxyethyl ether
• Her
• NSC 36391
• TL4N
• «beta»,«beta»'-Dihydroxydiethyl ether
• «beta»,«beta»'-Dihydroxyethyl ether
• «beta»,«beta»'-Dihydroxydiethyl ether
• «beta»,«beta»'-Dihydroxyethyl ether

• 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).
• 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).
• 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).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ΔcH°liquid	[-2374.70; -2372.90]	kJ/mol
ΔcH°liquid	-2374.70 ± 2.40	kJ/mol	NIST
ΔcH°liquid	-2372.90	kJ/mol	NIST
ΔfG°	-395.84	kJ/mol	Joback Calculated Property
ΔfH°gas	-571.50	kJ/mol	KDB
ΔfH°liquid	-628.50 ± 2.40	kJ/mol	NIST
ΔfusH°	15.48	kJ/mol	Joback Calculated Property
ΔvapH°	60.27	kJ/mol	Joback Calculated Property
log10WS	0.89		Crippen Calculated Property
logPoct/wat	-1.012		Crippen Calculated Property
McVol	84.830	ml/mol	McGowan Calculated Property
Pc	[4700.00; 4770.00]	kPa
Pc	4700.00	kPa	KDB
Pc	4770.00 ± 50.00	kPa	NIST
Inp	[925.00; 967.00]
Inp	927.00		NIST
Inp	925.00		NIST
Inp	967.00		NIST
Inp	941.00		NIST
I	[1953.00; 1989.00]
I	1989.00		NIST
I	1975.00		NIST
I	1968.00		NIST
I	1953.00		NIST
I	1975.00		NIST
Tboil	519.00	K	KDB
Tc	[680.00; 753.00]	K
Tc	681.00	K	KDB
Tc	753.00	K	Critica...
Tc	753.00 ± 4.00	K	NIST
Tc	723.50 ± 50.00	K	NIST
Tc	680.00 ± 20.00	K	NIST
Tfus	[262.80; 265.40]	K
Tfus	265.00	K	KDB
Tfus	265.35	K	NIST
Tfus	265.40 ± 0.60	K	NIST
Tfus	263.05 ± 0.50	K	NIST
Tfus	262.80 ± 0.10	K	NIST
Vc	0.316	m3/kmol	Joback Calculated Property
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[193.32; 228.87]	J/mol×K	[497.70; 656.34]
Cp,gas	193.32	J/mol×K	497.70	Joback Calculated Property
Cp,gas	199.74	J/mol×K	524.14	Joback Calculated Property
Cp,gas	205.96	J/mol×K	550.58	Joback Calculated Property
Cp,gas	211.98	J/mol×K	577.02	Joback Calculated Property
Cp,gas	217.81	J/mol×K	603.46	Joback Calculated Property
Cp,gas	223.44	J/mol×K	629.90	Joback Calculated Property
Cp,gas	228.87	J/mol×K	656.34	Joback Calculated Property
Cp,liquid	[243.90; 287.00]	J/mol×K	[298.00; 353.15]
Cp,liquid	243.90	J/mol×K	298.00	NIST
Cp,liquid	287.00	J/mol×K	298.00	NIST
Cp,liquid	248.20	J/mol×K	303.15	Heat ca...
Cp,liquid	251.30	J/mol×K	313.15	Heat ca...
Cp,liquid	255.00	J/mol×K	323.15	Heat ca...
Cp,liquid	259.20	J/mol×K	333.15	Heat ca...
Cp,liquid	263.80	J/mol×K	343.15	Heat ca...
Cp,liquid	266.80	J/mol×K	353.15	Heat ca...
η	[0.0007890; 0.0381100]	Pa×s	[293.15; 464.05]
η	0.0364330	Pa×s	293.15	Supplem...
η	0.0365200	Pa×s	293.15	Experim...
η	0.0381100	Pa×s	293.20	Phase e...
η	0.0351000	Pa×s	294.20	Density...
η	0.0283600	Pa×s	298.15	Experim...
η	0.0300120	Pa×s	298.15	Densiti...
η	0.0300120	Pa×s	298.15	Thermop...
η	0.0298200	Pa×s	298.20	Phase e...
η	0.0220910	Pa×s	303.15	Supplem...
η	0.0221560	Pa×s	303.15	Densiti...
η	0.0236400	Pa×s	303.20	Phase e...
η	0.0179340	Pa×s	308.15	Densiti...
η	0.0169720	Pa×s	308.15	Densiti...
η	0.0169720	Pa×s	308.15	Thermop...
η	0.0190200	Pa×s	308.20	Phase e...
η	0.0152500	Pa×s	312.60	Experim...
η	0.0151000	Pa×s	313.05	Density...
η	0.0147060	Pa×s	313.15	Densiti...
η	0.0145630	Pa×s	313.15	Supplem...
η	0.0156000	Pa×s	313.20	Phase e...
η	0.0121910	Pa×s	318.15	Densiti...
η	0.0126900	Pa×s	318.20	Phase e...
η	0.0100290	Pa×s	323.15	Supplem...
η	0.0101950	Pa×s	323.15	Densiti...
η	0.0106200	Pa×s	323.20	Phase e...
η	0.0088530	Pa×s	328.20	Phase e...
η	0.0084580	Pa×s	329.28	Experim...
η	0.0076400	Pa×s	333.05	Density...
η	0.0072200	Pa×s	333.15	Supplem...
η	0.0073620	Pa×s	333.20	Phase e...
η	0.0062080	Pa×s	338.20	Phase e...
η	0.0053690	Pa×s	343.15	Supplem...
η	0.0053240	Pa×s	343.20	Phase e...
η	0.0053400	Pa×s	344.99	Experim...
η	0.0048090	Pa×s	349.77	Experim...
η	0.0044100	Pa×s	353.05	Density...
η	0.0041390	Pa×s	353.15	Supplem...
η	0.0032310	Pa×s	366.77	Experim...
η	0.0027600	Pa×s	373.60	Density...
η	0.0019200	Pa×s	393.40	Density...
η	0.0014100	Pa×s	413.25	Density...
η	0.0014090	Pa×s	413.65	Experim...
η	0.0011500	Pa×s	428.15	Density...
η	0.0007890	Pa×s	464.05	Experim...
ΔvapH	[55.10; 69.20]	kJ/mol	[273.00; 523.00]
ΔvapH	57.30 ± 5.90	kJ/mol	273.00	NIST
ΔvapH	66.50	kJ/mol	413.00	NIST
ΔvapH	59.80	kJ/mol	441.00	NIST
ΔvapH	69.20	kJ/mol	458.00	NIST
ΔvapH	66.80	kJ/mol	462.50	NIST
ΔvapH	63.10 ± 0.30	kJ/mol	474.50	NIST
ΔvapH	55.10 ± 0.50	kJ/mol	474.50	NIST
ΔvapH	66.90 ± 0.30	kJ/mol	474.50	NIST
ΔvapH	59.20 ± 0.30	kJ/mol	474.50	NIST
ΔvapH	66.57	kJ/mol	523.00	NIST
n0	1.44724		293.15	Liquid-...
ρl	[1059.00; 1123.30]	kg/m3	[283.15; 373.15]
ρl	1123.30	kg/m3	283.15	Thermop...
ρl	1121.40	kg/m3	288.15	Thermop...
ρl	1120.30	kg/m3	288.15	Activit...
ρl	1120.05	kg/m3	288.15	Activit...
ρl	1119.80	kg/m3	288.15	Thermop...
ρl	1116.00	kg/m3	293.00	KDB
ρl	1116.50	kg/m3	293.15	Measure...
ρl	1117.80	kg/m3	293.15	Thermop...
ρl	1116.73	kg/m3	293.15	Thermod...
ρl	1116.20	kg/m3	293.15	Thermop...
ρl	1109.16	kg/m3	298.00	Removal...
ρl	1112.38	kg/m3	298.15	Thermod...
ρl	1114.20	kg/m3	298.15	Thermop...
ρl	1113.00	kg/m3	298.15	Solubil...
ρl	1112.70	kg/m3	298.15	Thermop...
ρl	1112.80	kg/m3	298.15	Density...
ρl	1112.38	kg/m3	298.15	Excess ...
ρl	1112.56	kg/m3	298.15	Isobari...
ρl	1112.70	kg/m3	298.15	Densiti...
ρl	1113.00	kg/m3	298.15	Measure...
ρl	1113.17	kg/m3	298.15	Thermod...
ρl	1109.40	kg/m3	303.15	Measure...
ρl	1110.00	kg/m3	303.15	Density...
ρl	1109.30	kg/m3	303.15	Densiti...
ρl	1109.10	kg/m3	303.15	Thermop...
ρl	1109.60	kg/m3	303.15	Thermod...
ρl	1109.20	kg/m3	303.15	Solubil...
ρl	1110.60	kg/m3	303.15	Thermop...
ρl	1109.20	kg/m3	303.15	Density...
ρl	1109.00	kg/m3	303.15	Vapour ...
ρl	1105.65	kg/m3	308.15	Excess ...
ρl	1105.90	kg/m3	308.15	Densiti...
ρl	1106.01	kg/m3	308.15	Thermod...
ρl	1105.65	kg/m3	308.15	Excess ...
ρl	1105.88	kg/m3	308.15	Excess ...
ρl	1106.10	kg/m3	308.15	Solubil...
ρl	1105.60	kg/m3	308.15	Density...
ρl	1107.00	kg/m3	308.15	Thermop...
ρl	1105.50	kg/m3	308.15	Thermop...
ρl	1105.80	kg/m3	308.15	Measure...
ρl	1105.88	kg/m3	308.15	Thermod...
ρl	1105.86	kg/m3	308.50	Excess ...
ρl	1103.00	kg/m3	313.15	Vapour ...
ρl	1101.90	kg/m3	313.15	Thermop...
ρl	1102.50	kg/m3	313.15	Densiti...
ρl	1103.40	kg/m3	313.15	Thermop...
ρl	1102.30	kg/m3	313.15	Density...
ρl	1103.00	kg/m3	313.15	Density...
ρl	1102.20	kg/m3	313.15	Measure...
ρl	1103.00	kg/m3	313.15	Solubil...
ρl	1099.30	kg/m3	318.15	Solubil...
ρl	1099.70	kg/m3	318.15	Thermop...
ρl	1099.20	kg/m3	318.15	Density...
ρl	1098.60	kg/m3	318.15	Measure...
ρl	1095.00	kg/m3	323.15	Measure...
ρl	1094.70	kg/m3	323.15	Thermop...
ρl	1095.90	kg/m3	323.15	Density...
ρl	1096.10	kg/m3	323.15	Thermop...
ρl	1095.00	kg/m3	323.15	Vapour ...
ρl	1091.40	kg/m3	328.15	Measure...
ρl	1092.50	kg/m3	328.15	Thermop...
ρl	1087.40	kg/m3	333.15	Thermop...
ρl	1087.70	kg/m3	333.15	Measure...
ρl	1088.50	kg/m3	333.15	Density...
ρl	1088.00	kg/m3	333.15	Vapour ...
ρl	1088.80	kg/m3	333.15	Thermop...
ρl	1084.00	kg/m3	338.15	Measure...
ρl	1085.20	kg/m3	338.15	Thermop...
ρl	1080.00	kg/m3	343.15	Thermop...
ρl	1081.00	kg/m3	343.15	Vapour ...
ρl	1081.50	kg/m3	343.15	Thermop...
ρl	1081.10	kg/m3	343.15	Density...
ρl	1080.30	kg/m3	343.15	Measure...
ρl	1077.80	kg/m3	348.15	Thermop...
ρl	1074.10	kg/m3	353.15	Thermop...
ρl	1070.30	kg/m3	358.15	Thermop...
ρl	1066.60	kg/m3	363.15	Thermop...
ρl	1062.80	kg/m3	368.15	Thermop...
ρl	1059.00	kg/m3	373.15	Thermop...
λ	[0.20; 0.21]	W/m×K	[298.10; 338.20]
λ	0.20	W/m×K	298.10	Applica...
λ	0.20	W/m×K	308.00	Applica...
λ	0.20	W/m×K	318.20	Applica...
λ	0.20	W/m×K	328.40	Applica...
λ	0.21	W/m×K	338.20	Applica...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	406.20	K	1.90	NIST

Datasets

1. Viscosity, Pa*s (2)
2. Mass density, kg/m3 (3)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	98.00	0.0365
293.15	49030.00	0.0527
293.15	98060.00	0.0742
293.15	147100.00	0.1026
293.15	196130.00	0.1399
293.15	245160.00	0.1873
298.15	98.00	0.0284
298.15	49030.00	0.0404
298.15	98060.00	0.0565
298.15	147100.00	0.0772
298.15	196130.00	0.1038
298.15	245160.00	0.1383
312.60	98.00	0.0152
312.62	49030.00	0.0210
312.63	98060.00	0.0282
312.67	147100.00	0.0371
312.71	196130.00	0.0483
312.75	245160.00	0.0621
329.28	98.00	0.0085
329.33	98060.00	0.0147
329.33	196130.00	0.0238
329.33	245160.00	0.0296
329.38	49030.00	0.0113
329.38	147100.00	0.0188
344.99	98.00	0.0053
345.20	49030.00	0.0071
345.38	98060.00	0.0090
345.47	147100.00	0.0112
345.61	196130.00	0.0138
345.78	245160.00	0.0168
349.77	98.00	0.0048
350.06	49030.00	0.0063
350.13	147100.00	0.0099
350.16	98060.00	0.0079
350.40	196130.00	0.0120
366.77	98.00	0.0032
367.13	49030.00	0.0041
367.26	147100.00	0.0063
367.30	98060.00	0.0051
367.37	196130.00	0.0076
367.61	245160.00	0.0091
413.65	98.00	0.0014
413.80	49030.00	0.0018
413.93	98060.00	0.0022
414.01	147100.00	0.0026
414.09	196130.00	0.0030
414.29	245160.00	0.0035
463.94	98060.00	0.0012
463.99	49030.00	0.0010
464.05	98.00	0.0008
464.09	147100.00	0.0014
464.20	196130.00	0.0017
464.37	245160.00	0.0019
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.30	308.15	0.0176
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1124.3
283.15	1000.00	1124.7
283.15	2000.00	1125.3
283.15	5000.00	1126.5
283.15	7000.00	1127.4
283.15	10000.00	1128.8
283.15	12000.00	1129.6
283.15	16000.00	1131.3
283.15	20000.00	1133.0
283.15	25000.00	1135.1
283.15	30000.00	1137.2
283.15	35000.00	1139.2
283.15	40000.00	1141.2
283.15	45000.00	1143.0
283.15	50000.00	1145.1
283.15	55000.00	1146.9
283.15	60000.00	1148.8
283.15	65000.00	1150.7
283.15	70000.00	1152.4
283.15	75000.00	1154.2
283.15	80000.00	1155.8
283.15	85000.00	1157.5
283.15	90000.00	1159.2
283.15	95000.00	1160.9
293.15	100.00	1117.1
293.15	1000.00	1117.5
293.15	2000.00	1118.0
293.15	5000.00	1119.3
293.15	7000.00	1120.2
293.15	10000.00	1121.6
293.15	12000.00	1122.5
293.15	16000.00	1124.3
293.15	20000.00	1126.0
293.15	25000.00	1128.2
293.15	30000.00	1130.3
293.15	35000.00	1132.4
293.15	40000.00	1134.3
293.15	45000.00	1136.4
293.15	50000.00	1138.4
293.15	55000.00	1140.4
293.15	60000.00	1142.2
293.15	65000.00	1144.1
293.15	70000.00	1145.8
293.15	75000.00	1147.7
293.15	80000.00	1149.4
293.15	85000.00	1151.2
293.15	90000.00	1152.9
293.15	95000.00	1154.6
303.14	100.00	1109.9
303.14	1000.00	1110.3
303.14	2000.00	1110.7
303.14	5000.00	1112.2
303.14	7000.00	1113.1
303.14	10000.00	1114.5
303.14	12000.00	1115.4
303.14	16000.00	1117.3
303.14	20000.00	1119.0
303.14	25000.00	1121.2
303.14	30000.00	1123.4
303.14	35000.00	1125.5
303.14	40000.00	1127.5
303.14	45000.00	1129.6
303.14	50000.00	1131.6
303.14	55000.00	1133.6
303.14	60000.00	1135.5
303.14	65000.00	1137.4
303.14	70000.00	1139.3
303.14	75000.00	1141.1
303.14	80000.00	1142.9
303.14	85000.00	1144.6
303.14	90000.00	1146.4
303.14	95000.00	1148.2
313.15	100.00	1102.7
313.15	1000.00	1103.2
313.15	2000.00	1103.6
313.15	5000.00	1105.2
313.15	7000.00	1106.2
313.15	10000.00	1107.7
313.15	12000.00	1108.6
313.15	16000.00	1110.4
313.15	20000.00	1112.3
313.15	25000.00	1114.5
313.15	30000.00	1116.7
313.15	35000.00	1118.9
313.15	40000.00	1121.0
313.15	45000.00	1123.1
313.15	50000.00	1125.1
313.15	55000.00	1127.1
313.15	60000.00	1129.1
313.15	65000.00	1131.1
313.15	70000.00	1132.9
313.15	75000.00	1134.8
313.15	80000.00	1136.6
313.15	85000.00	1138.4
313.15	90000.00	1140.2
313.15	95000.00	1141.9
323.20	100.00	1095.4
323.20	1000.00	1095.8
323.20	2000.00	1096.3
323.20	5000.00	1097.8
323.20	7000.00	1098.8
323.20	10000.00	1100.3
323.20	12000.00	1101.3
323.20	16000.00	1103.3
323.20	20000.00	1105.2
323.20	25000.00	1107.5
323.20	30000.00	1109.9
323.20	35000.00	1112.0
323.20	40000.00	1114.2
323.20	45000.00	1116.3
323.20	50000.00	1118.4
323.20	55000.00	1120.5
323.20	60000.00	1122.5
323.20	65000.00	1124.5
323.20	70000.00	1126.5
323.20	75000.00	1128.3
323.20	80000.00	1130.3
323.20	85000.00	1132.2
323.20	90000.00	1133.9
323.20	95000.00	1135.7
333.20	100.00	1088.1
333.20	1000.00	1088.7
333.20	2000.00	1089.2
333.20	5000.00	1090.8
333.20	7000.00	1091.8
333.20	10000.00	1093.3
333.20	12000.00	1094.4
333.20	16000.00	1096.4
333.20	20000.00	1098.3
333.20	25000.00	1100.7
333.20	30000.00	1103.0
333.20	35000.00	1105.3
333.20	40000.00	1107.6
333.20	45000.00	1109.7
333.20	50000.00	1111.9
333.20	55000.00	1113.9
333.20	60000.00	1116.0
333.20	65000.00	1118.0
333.20	70000.00	1120.1
333.20	75000.00	1121.9
333.20	80000.00	1123.8
333.20	85000.00	1125.9
333.20	90000.00	1127.7
333.20	95000.00	1129.5
343.20	100.00	1080.7
343.20	1000.00	1081.2
343.20	2000.00	1081.7
343.20	5000.00	1083.4
343.20	7000.00	1084.5
343.20	10000.00	1086.1
343.20	12000.00	1087.1
343.20	16000.00	1089.1
343.20	20000.00	1091.2
343.20	25000.00	1093.7
343.20	30000.00	1096.1
343.20	35000.00	1098.5
343.20	40000.00	1100.8
343.20	45000.00	1103.1
343.20	50000.00	1105.2
343.20	55000.00	1107.4
343.20	60000.00	1109.5
343.20	65000.00	1111.6
343.20	70000.00	1113.7
343.20	75000.00	1115.7
343.20	80000.00	1117.6
343.20	85000.00	1119.5
343.20	90000.00	1121.4
343.20	95000.00	1123.3
353.19	100.00	1073.2
353.19	1000.00	1073.8
353.19	2000.00	1074.3
353.19	5000.00	1076.0
353.19	7000.00	1077.1
353.19	10000.00	1078.7
353.19	12000.00	1079.8
353.19	16000.00	1081.9
353.19	20000.00	1084.0
353.19	25000.00	1086.6
353.19	30000.00	1089.1
353.19	35000.00	1091.6
353.19	40000.00	1093.9
353.19	45000.00	1096.3
353.19	50000.00	1098.5
353.19	55000.00	1100.8
353.19	60000.00	1102.9
353.19	65000.00	1105.0
353.19	70000.00	1107.2
353.19	75000.00	1109.2
353.19	80000.00	1111.2
353.19	85000.00	1113.2
353.19	90000.00	1115.1
353.19	95000.00	1117.0
363.17	100.00	1065.6
363.17	1000.00	1066.2
363.17	2000.00	1066.8
363.17	5000.00	1068.5
363.17	7000.00	1069.6
363.17	10000.00	1071.4
363.17	12000.00	1072.5
363.17	16000.00	1074.6
363.17	20000.00	1076.9
363.17	25000.00	1079.4
363.17	30000.00	1082.0
363.17	35000.00	1084.6
363.17	40000.00	1087.0
363.17	45000.00	1089.4
363.17	50000.00	1091.8
363.17	55000.00	1094.1
363.17	60000.00	1096.3
363.17	65000.00	1098.5
363.17	70000.00	1100.5
363.17	75000.00	1102.6
363.17	80000.00	1104.8
363.17	85000.00	1106.8
363.17	90000.00	1108.8
363.17	95000.00	1110.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1123.1
283.15	100.00	1123.1
283.15	640.00	1123.3
283.15	1080.00	1123.5
283.15	1590.00	1123.7
283.15	2140.00	1124.0
283.15	3050.00	1124.3
283.15	5050.00	1125.2
283.15	6930.00	1126.0
283.15	9930.00	1127.2
283.15	14810.00	1129.3
283.15	19760.00	1131.3
283.15	24610.00	1133.3
283.15	29600.00	1135.2
283.15	34500.00	1137.1
283.15	39420.00	1139.0
283.15	44300.00	1140.8
283.15	49180.00	1142.6
283.15	54060.00	1144.4
283.15	59030.00	1146.1
283.15	63810.00	1147.8
283.15	68760.00	1149.5
293.15	100.00	1115.9
293.15	100.00	1115.9
293.15	570.00	1116.1
293.15	1080.00	1116.3
293.15	1530.00	1116.6
293.15	2110.00	1116.8
293.15	3080.00	1117.2
293.15	5040.00	1118.1
293.15	6990.00	1118.9
293.15	9940.00	1120.2
293.15	14840.00	1122.3
293.15	19740.00	1124.3
293.15	24680.00	1126.4
293.15	29600.00	1128.4
293.15	34530.00	1130.3
293.15	39360.00	1132.2
293.15	44320.00	1134.1
293.15	49120.00	1136.0
293.15	54090.00	1137.8
293.15	58990.00	1139.6
293.15	63820.00	1141.3
293.15	68750.00	1143.0
303.15	100.00	1108.8
303.15	100.00	1108.8
303.15	680.00	1109.0
303.15	1130.00	1109.2
303.15	1580.00	1109.4
303.15	2120.00	1109.7
303.15	3030.00	1110.1
303.15	5040.00	1111.0
303.15	6950.00	1111.9
303.15	9960.00	1113.2
303.15	14840.00	1115.4
303.15	19740.00	1117.5
303.15	24680.00	1119.6
303.15	29610.00	1121.6
303.15	34520.00	1123.6
303.15	39380.00	1125.6
303.15	44350.00	1127.5
303.15	49140.00	1129.4
303.15	54090.00	1131.3
303.15	58990.00	1133.1
303.15	63850.00	1134.9
303.15	68760.00	1136.6
313.15	100.00	1101.7
313.15	100.00	1101.6
313.15	640.00	1101.8
313.15	1140.00	1102.1
313.15	1640.00	1102.3
313.15	2100.00	1102.5
313.15	3090.00	1103.0
313.15	5130.00	1103.9
313.15	6960.00	1104.8
313.15	9960.00	1106.1
313.15	14940.00	1108.4
313.15	19750.00	1110.6
313.15	24640.00	1112.7
313.15	29640.00	1114.8
313.15	34510.00	1116.9
313.15	39340.00	1118.9
313.15	44340.00	1120.9
313.15	49190.00	1123.2
313.15	54020.00	1124.7
313.15	59030.00	1126.7
313.15	63880.00	1128.5
313.15	68820.00	1130.3
323.15	100.00	1094.3
323.15	100.00	1094.3
323.15	680.00	1094.6
323.15	1130.00	1094.8
323.15	1570.00	1095.0
323.15	2100.00	1095.2
323.15	3080.00	1095.7
323.15	5080.00	1096.7
323.15	7000.00	1097.6
323.15	9950.00	1099.0
323.15	14890.00	1101.4
323.15	19770.00	1103.6
323.15	24680.00	1105.8
323.15	29600.00	1108.0
323.15	34530.00	1110.1
323.15	39360.00	1112.2
323.15	44290.00	1114.3
323.15	49260.00	1116.3
323.15	54100.00	1118.2
323.15	59060.00	1120.2
323.15	63880.00	1122.0
323.15	68770.00	1123.8
333.15	100.00	1087.0
333.15	100.00	1087.0
333.15	660.00	1087.3
333.15	1120.00	1087.5
333.15	1630.00	1087.8
333.15	2100.00	1088.0
333.15	3070.00	1088.5
333.15	5060.00	1089.5
333.15	7050.00	1090.5
333.15	9930.00	1091.9
333.15	14780.00	1094.3
333.15	19770.00	1096.7
333.15	24660.00	1099.0
333.15	29540.00	1101.2
333.15	34500.00	1103.4
333.15	39330.00	1105.5
333.15	44230.00	1107.6
333.15	49130.00	1109.7
333.15	54060.00	1111.7
333.15	59020.00	1113.7
333.15	63840.00	1115.7
333.15	68830.00	1117.5
343.15	100.00	1079.7
343.15	100.00	1079.7
343.15	670.00	1080.0
343.15	1100.00	1080.2
343.15	1520.00	1080.4
343.15	2120.00	1080.7
343.15	3060.00	1081.2
343.15	5040.00	1082.3
343.15	6970.00	1083.3
343.15	9950.00	1084.8
343.15	14870.00	1087.3
343.15	19740.00	1089.6
343.15	24710.00	1092.1
343.15	29560.00	1094.4
343.15	34490.00	1096.6
343.15	39350.00	1098.8
343.15	44290.00	1101.0
343.15	49180.00	1103.1
343.15	54070.00	1105.2
343.15	58980.00	1107.3
343.15	63910.00	1109.3
343.15	68720.00	1111.2
353.15	100.00	1072.2
353.15	100.00	1072.2
353.15	560.00	1072.5
353.15	1090.00	1072.8
353.15	1550.00	1073.0
353.15	2080.00	1073.3
353.15	3040.00	1073.8
353.15	5060.00	1074.9
353.15	7020.00	1076.0
353.15	9970.00	1077.5
353.15	14830.00	1080.1
353.15	19740.00	1082.6
353.15	24680.00	1085.1
353.15	29560.00	1087.5
353.15	34550.00	1089.8
353.15	39420.00	1092.1
353.15	44280.00	1094.3
353.15	49230.00	1096.5
353.15	54110.00	1098.7
353.15	59020.00	1100.8
353.15	64010.00	1102.9
353.15	68770.00	1104.8
363.08	100.00	1064.5
363.08	100.00	1064.4
363.08	620.00	1064.7
363.08	1110.00	1065.0
363.08	1570.00	1065.2
363.08	2100.00	1065.5
363.08	3020.00	1066.0
363.08	5070.00	1067.2
363.08	7000.00	1068.3
363.08	9970.00	1069.9
363.08	14840.00	1072.6
363.08	19750.00	1075.1
363.08	24660.00	1077.7
363.08	29610.00	1080.2
363.08	34480.00	1082.6
363.08	39400.00	1084.9
363.08	44290.00	1087.2
363.08	49160.00	1089.5
363.08	54110.00	1091.7
363.08	58990.00	1093.9
363.08	63880.00	1096.0
363.08	68760.00	1098.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	989.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[396.81; 548.09]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.56166e+01
Coefficient B			-4.75686e+03
Coefficient C			-8.64930e+01
Temperature range, min.			396.81
Temperature range, max.			548.09
Pvap	1.33	kPa	396.81	Calculated Property
Pvap	2.93	kPa	413.62	Calculated Property
Pvap	5.97	kPa	430.43	Calculated Property
Pvap	11.36	kPa	447.24	Calculated Property
Pvap	20.44	kPa	464.05	Calculated Property
Pvap	34.97	kPa	480.85	Calculated Property
Pvap	57.26	kPa	497.66	Calculated Property
Pvap	90.19	kPa	514.47	Calculated Property
Pvap	137.28	kPa	531.28	Calculated Property
Pvap	202.64	kPa	548.09	Calculated Property
Pvap	[1.07e-05; 4415.80]	kPa	[262.70; 744.60]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.08791e+02
Coefficient B			-1.28556e+04
Coefficient C			-1.28373e+01
Coefficient D			3.16995e-06
Temperature range, min.			262.70
Temperature range, max.			744.60
Pvap	1.07e-05	kPa	262.70	Calculated Property
Pvap	4.34e-03	kPa	316.24	Calculated Property
Pvap	0.24	kPa	369.79	Calculated Property
Pvap	3.86	kPa	423.33	Calculated Property
Pvap	29.48	kPa	476.88	Calculated Property
Pvap	135.63	kPa	530.42	Calculated Property
Pvap	439.99	kPa	583.97	Calculated Property
Pvap	1115.30	kPa	637.51	Calculated Property
Pvap	2367.36	kPa	691.06	Calculated Property
Pvap	4415.80	kPa	744.60	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol, 2,2'-oxybis-.

Mixtures

• Benzene, nitro- + Ethanol, 2,2'-oxybis-
• 1-Butanol + Ethanol, 2,2'-oxybis-
• 1,4-Butanediol + Ethanol, 2,2'-oxybis-
• Ethanol, 2,2'-oxybis- + Thiophene, tetrahydro-, 1,1-dioxide
• 1,2-Ethanediol + Ethanol, 2,2'-oxybis-
• Triethylene glycol + Ethanol, 2,2'-oxybis-
• 1,2-Ethanediol + Triethylene glycol + Ethanol, 2,2'-oxybis-
• Nitrogen + Sulfur dioxide + Ethanol, 2,2'-oxybis-
• Formamide, N,N-dimethyl- + Ethanol, 2,2'-oxybis-
• Sulfur dioxide + Ethanol, 2,2'-oxybis-
• Formamide, N,N-dimethyl- + Sulfur dioxide + Ethanol, 2,2'-oxybis-
• Toluene + Decane + Ethanol, 2,2'-oxybis-
• Ethanol, 2,2'-oxybis- + lithium chloride + Water
• lithium bromide + Ethanol, 2,2'-oxybis- + Water
• Ethanol, 2,2'-oxybis- + Tromethamine + Water
• Ethanol, 2,2'-oxybis- + Pentane
• n-Hexane + Ethanol, 2,2'-oxybis-
• Heptane + Ethanol, 2,2'-oxybis-
• Octane + Ethanol, 2,2'-oxybis-
• Ethanol, 2,2'-oxybis- + Nonane

Find more mixtures with Ethanol, 2,2'-oxybis-.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Crippen Method
• Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
• Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
• Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
• Mutual diffusion coefficients of aqueous solutions of some glycols
• Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 465 K and at high pressures up to 245 MPa
• The effect of the end group, molecular weight and size on the solubility of compounds in supercritical carbon dioxide
• Experimental study and phase equilibrium modeling of systems containing acid gas and glycol
• Solubility for dilute sulfur dioxide, viscosities, excess properties, and viscous flow thermodynamics of binary system N, N-dimethylformamide + diethylene glycol
• Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
• Thermodynamic properties and spectral investigation of dilute sulfur dioxide in binary system N,N-dimethylformamide + diethylene glycol
• Determination and modeling of binary and ternary solid-liquid phase equilibrium for the systems formed by adipic acid, urea and diethylene glycol
• Separation of methane/ethylene gas mixtures efficiently by using ZIF- 67/water-ethylene glycol slurry
• Liquid-liquid equilibrium in binary and ternary mixtures containing formaldehyde, water, methanol, methylal, and poly(oxymethylene) dimethyl ethers
• New measurements and modeling of high pressure thermodynamic properties of glycols
• Critical temperatures and pressures of ethylene glycols
• Viscosity of liquid diethylene, triethylene and tetraethylene glycols at moderately high pressures using a vibrating wire instrument
• Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
• The experimental study on the influence of crown ethers and glycols on the mutual solubility of lithium bromide in water
• Vapour pressures and densities of the mixed-solvent desiccants (glycols + water + salts)
• Densities and vapor pressures of mixed-solvent desiccant systems containing {glycol (diethylene, or triethylene, or tetraethylene glycol) + salt (magnesium chloride) + water}
• Experimental and predicted refractive index properties in ternary mixtures of associated liquids
• Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
• Molar heat capacities of some aqueous 2-amino-2-hydroxymethyl-1,3-propanediol + glycol systems
• Thermophysical property characterization of ternary system containing {glycol (DEG/TEG/T4EG) + 2-amino-2-hydroxymethyl-1,3-propanediol + water}
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Solubilities and thermodynamic properties of CO2 in choline-chloride based deep eutectic solvents
• Liquid-liquid equilibria for ternary systems polyoxymethylene dimethyl ethers + para-xylene + water
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Binary and ternary solid-liquid phase equilibrium for the systems formed by succinic acid, urea and diethylene glycol: Determination and modelling
• Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
• Densities and viscosities for binary mixtures of polyoxymethylene dimethyl ethers with different CH2O chain length n = 2, 3, 4 at different temperatures
• Thermal stability analysis, experimental conductivity and pH of phosphonium-based deep eutectic solvents and their prediction by a new empirical equation
• Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
• Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
• Volumetric and ultrasonic studies on interactions of ethylene glycol, diethylene glycol and triethylene glycol in aqueous solutions of glycerol at temperatures T = (293.15 K - 308.15) K
• Acoustic and thermodynamic study of D-Panthenol in aqueous solutions of glycol at different temperatures
• Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
• Excess molar enthalpies of binary mixtures containing ethylene glycols or poly(ethylene glycols) + ethyl alcohol at 308.15K and atmospheric pressure
• Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
• Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
• Heat Capacity of Several Mixed-Solvent Desiccants Containing Glycol + Water + MgCl2
• Molar heat capacity of several aqueous solutions of n-[tris(hydroxymethyl)methyl-3-amino]- propanesulfonic acid (TAPS) + glycol
• Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Four Poly(Ethylene Glycols) at Infinite Dilution in Water at Temperatures T = (278 to 343) K and Atmospheric Pressure
• Thermophysical properties of glycols and glymes
• Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
• Investigation on Temperature-Dependent Volumetric and Acoustical Properties of Homologous Series of Glycols in Aqueous Sorbitol Solutions
• Solubility of Carbon Dioxide in Poly(oxymethylene) Dimethyl Ethers
• Measurement and Modeling of Isobaric Vapor-Liquid Equilibrium of Water + Glycols
• Thermodynamic and Kinetic Studies of CO2 Capture by Glycol and Amine-Based Deep Eutectic Solvents
• Thermodynamic Interactions Study of Some Ethylene Glycols in Aqueous Aniline Solutions at Different Temperatures: An Acoustical and Volumetric Approach
• Solubility of Acetylene in Alcohols and Ketones
• Effect of Ethylene, Diethylene, and Triethylene Glycols and Glycerol on the Physicochemical Properties and Phase Behavior of Benzyltrimethyl and Benzyltributylammonium Chloride Based Deep Eutectic Solvents at 283.15-343.15 K
• Measurement and Thermodynamic Models for Ternary Liquid-Liquid Equilibrium Systems {Water + Polyoxymethylene Dimethyl Ethers +4-Methyl-2-pentanol} at Different Temperatures
• Experimental Isobaric Vapor Liquid Equilibrium for Binary Systems Diethylene Glycol Dibenzoate + Diethylene Glycol, Diethylene Glycol Dibenzoate + Octyl Benzoate, and Ternary System Diethylene Glycol Dibenzoate + Diethylene Glycol + Octyl Benzoate at 1.0152 kPa
• Liquid-Liquid Equilibrium for Ternary Systems of Polyoxymethylene Dimethyl Ethers + o-Xylene + Water at 293.15 K
• Solubility of 4-Chloro-2,5-dimethoxynitrobenzene, 4-Chloro-2,5-dimethoxyaniline, and 2,5-Dimethoxyaniline in Binary and Pure Solvents: Determination and Modeling
• Salting Effect of Sodium Hydroxide and Sodium Formate on the Liquid-Liquid Equilibrium of Polyoxymethylene Dimethyl Ethers in Aqueous Solution
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Experimental and Correlated Liquid-Liquid Equilibrium Data for Ternary Systems (Water + Poly(oxymethylene) Dimethyl Ethers + Toluene) at T = 293.15 and 303.15 K and p = 101.3 kPa
• Densities, Viscosities, and Excess Properties for Binary Mixtures of Some Glycols and Polyglycols in N-Methylacetamide at 308.15 K
• Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
• Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
• Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
• Liquid-Liquid Equilibrium for the System Heptane + o-Xylene + Diethylene Glycol over the Temperature Range of 288.15 K to 318.15 K
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
• Solubility of Ethane in Diethylene Glycol
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
• Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
• Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
• Measurement and Correlation of the Solubility of Disodium 4,4?-Dinitrostilbene-2,2?-disulfonate in Aqueous Organic Solutions
• Measurement and Prediction of Excess Enthalpies for Ternary Solutions 1-Ethyl-3-methylimidazolium Dimethylphosphate + Methanol or Ethanol + Water at 298.15 K and at Normal Atmospheric Pressure
• Isobaric Vapor-Liquid Equilibrium for Four Binary Systems of Ethane-1,2-diol, Butane-1,4-diol, 2-(2- Hydroxyethoxy)ethan-1-ol and 2-[2-(2- Hydroxyethoxy)ethoxy]ethanol at 10.0 kPa, 20.0 kPa and 40.0 kPa
• Solubility of CO2 in Nonaqueous Absorption System of 2-(2-Aminoethylamine)ethanol + Benzyl Alcohol
• Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
• Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
• Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
• Solubility Comparison of Bis(2-hydroxyethyl) Ether and Tetraethylene Glycol before and after End-Group Modification by Ethyl Oxalyl Chloride in Supercritical Carbon Dioxide
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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