Mixture of Ethanol, 2,2'-oxybis- + Water

Datasets

1. Mass fraction (4)
2. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol
3. η - Viscosity, Pa*s (4)
4. Excess molar enthalpy (molar enthalpy (2)
5. n₀ - Refractive index (Na D-line)
6. ρ_l - Mass density, kg/m3 (9)
7. c_sound,fluid - Speed of Sound, m/s (6)
8. T_boil(P) - Boiling temperature at pressure P, K
9. λ_liquid - Thermal conductivity, W/m/K
10. Binary diffusion coefficient, m2/s (2)

Mass fraction of Ethanol, 2,2'-oxybis- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Ethanol, 2,2'-oxybis- (1) - Liquid mixture 1
280.25	0.9696
293.75	0.9568
302.65	0.9536
310.55	0.9469
320.95	0.9429
329.85	0.9376
340.00	0.9259
301.35	0.9565

Mass fraction of Ethanol, 2,2'-oxybis- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass fraction of Ethanol, 2,2'-oxybis- (1) - Liquid mixture 2
280.25	0.3192
293.75	0.3193
302.65	0.3157
310.55	0.3158
320.95	0.3185
329.85	0.3276
340.00	0.3494
301.35	0.3164

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 1
293.15	0.6783
308.15	0.6869
308.15	0.6821
293.15	0.6770

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 2
293.15	0.0428
308.15	0.0542
308.15	0.0539
293.15	0.0430

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.2000	303.15	111.80
0.2000	313.15	113.50
0.2000	323.15	115.30
0.2000	333.15	117.40
0.2000	343.15	119.30
0.2000	353.15	121.70
0.4000	303.15	148.70
0.4000	313.15	150.70
0.4000	323.15	153.30
0.4000	333.15	155.90
0.4000	343.15	158.70
0.4000	353.15	161.80
0.5000	303.15	167.60
0.5000	313.15	169.90
0.5000	323.15	172.60
0.5000	333.15	175.50
0.5000	343.15	178.70
0.5000	353.15	182.20
0.6000	303.15	184.50
0.6000	313.15	187.10
0.6000	323.15	190.30
0.6000	333.15	193.60
0.6000	343.15	197.30
0.6000	353.15	201.20
0.8000	303.15	217.90
0.8000	313.15	221.20
0.8000	323.15	225.00
0.8000	333.15	229.10
0.8000	343.15	233.60
0.8000	353.15	238.50

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0490	0.0021
293.15	0.0992	0.0036
293.15	0.1490	0.0055
293.15	0.1998	0.0077
293.15	0.2490	0.0100
293.15	0.2987	0.0125
293.15	0.3501	0.0152
293.15	0.4007	0.0177
293.15	0.4504	0.0201
293.15	0.4973	0.0223
293.15	0.5530	0.0247
293.15	0.5938	0.0262
293.15	0.6514	0.0283
293.15	0.6864	0.0295
293.15	0.7556	0.0314
293.15	0.7999	0.0324
293.15	0.8525	0.0335
293.15	0.9002	0.0344
293.15	0.9554	0.0353
298.15	0.0490	0.0017
298.15	0.0992	0.0029
298.15	0.1490	0.0043
298.15	0.1998	0.0060
298.15	0.2490	0.0078
298.15	0.2987	0.0098
298.15	0.3501	0.0118
298.15	0.4007	0.0137
298.15	0.4504	0.0156
298.15	0.4973	0.0172
298.15	0.5530	0.0191
298.15	0.5938	0.0202
298.15	0.6514	0.0219
298.15	0.6864	0.0227
298.15	0.7556	0.0242
298.15	0.7999	0.0249
298.15	0.8525	0.0258
298.15	0.9002	0.0265
298.15	0.9554	0.0272
303.15	0.0490	0.0016
303.15	0.0992	0.0026
303.15	0.1490	0.0038
303.15	0.1998	0.0053
303.15	0.2490	0.0068
303.15	0.2987	0.0083
303.15	0.3501	0.0100
303.15	0.4007	0.0115
303.15	0.4504	0.0130
303.15	0.4973	0.0143
303.15	0.5530	0.0157
303.15	0.5938	0.0166
303.15	0.6514	0.0179
303.15	0.6864	0.0186
303.15	0.7556	0.0197
303.15	0.7999	0.0203
303.15	0.8525	0.0210
303.15	0.9002	0.0216
303.15	0.9554	0.0221
308.15	0.0490	0.0014
308.15	0.0992	0.0023
308.15	0.1490	0.0033
308.15	0.1998	0.0045
308.15	0.2490	0.0058
308.15	0.2987	0.0071
308.15	0.3501	0.0084
308.15	0.4007	0.0096
308.15	0.4504	0.0108
308.15	0.4973	0.0118
308.15	0.5530	0.0129
308.15	0.5938	0.0137
308.15	0.6514	0.0147
308.15	0.6864	0.0152
308.15	0.7556	0.0161
308.15	0.7999	0.0166
308.15	0.8525	0.0171
308.15	0.9002	0.0175
308.15	0.9554	0.0179
293.15	0.0000	0.0011
298.15	0.0000	0.0009
303.15	0.0000	0.0008
308.15	0.0000	0.0008
293.15	1.0000	0.0359
298.15	1.0000	0.0277
303.15	1.0000	0.0225
308.15	1.0000	0.0183

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0010
293.15	0.0255	0.0014
293.15	0.0565	0.0022
293.15	0.1027	0.0036
293.15	0.1966	0.0075
293.15	0.3010	0.0126
293.15	0.3989	0.0175
293.15	0.5006	0.0222
293.15	0.6011	0.0260
293.15	0.7003	0.0295
293.15	0.8051	0.0323
293.15	0.8920	0.0340
293.15	1.0000	0.0364
303.15	0.0000	0.0008
303.15	0.0255	0.0011
303.15	0.0565	0.0017
303.15	0.1027	0.0026
303.15	0.1966	0.0051
303.15	0.3010	0.0084
303.15	0.3989	0.0114
303.15	0.5006	0.0141
303.15	0.6011	0.0163
303.15	0.7003	0.0185
303.15	0.8051	0.0200
303.15	0.8920	0.0212
303.15	1.0000	0.0221
313.15	0.0000	0.0007
313.15	0.0255	0.0010
313.15	0.0565	0.0013
313.15	0.1027	0.0020
313.15	0.1966	0.0037
313.15	0.3010	0.0058
313.15	0.3989	0.0078
313.15	0.5006	0.0095
313.15	0.6011	0.0109
313.15	0.7003	0.0122
313.15	0.8051	0.0132
313.15	0.8920	0.0139
313.15	1.0000	0.0146
323.15	0.0000	0.0006
323.15	0.0255	0.0008
323.15	0.0565	0.0010
323.15	0.1027	0.0015
323.15	0.1966	0.0028
323.15	0.3010	0.0042
323.15	0.3989	0.0055
323.15	0.5006	0.0067
323.15	0.6011	0.0076
323.15	0.7003	0.0085
323.15	0.8051	0.0091
323.15	0.8920	0.0096
323.15	1.0000	0.0100
333.15	0.0000	0.0005
333.15	0.0255	0.0006
333.15	0.0565	0.0008
333.15	0.1027	0.0012
333.15	0.1966	0.0021
333.15	0.3010	0.0032
333.15	0.3989	0.0041
333.15	0.5006	0.0049
333.15	0.6011	0.0055
333.15	0.7003	0.0061
333.15	0.8051	0.0065
333.15	0.8920	0.0069
333.15	1.0000	0.0072
343.15	0.0000	0.0004
343.15	0.0255	0.0005
343.15	0.0565	0.0007
343.15	0.1027	0.0010
343.15	0.1966	0.0017
343.15	0.3010	0.0025
343.15	0.3989	0.0032
343.15	0.5006	0.0037
343.15	0.6011	0.0042
343.15	0.7003	0.0046
343.15	0.8051	0.0049
343.15	0.8920	0.0051
343.15	1.0000	0.0054
353.15	0.0000	0.0004
353.15	0.0255	0.0005
353.15	0.0565	0.0006
353.15	0.1027	0.0008
353.15	0.1966	0.0014
353.15	0.3010	0.0020
353.15	0.3989	0.0025
353.15	0.5006	0.0029
353.15	0.6011	0.0033
353.15	0.7003	0.0036
353.15	0.8051	0.0038
353.15	0.8920	0.0040
353.15	1.0000	0.0041

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.2500	294.25	0.0098
0.2500	313.05	0.0049
0.2500	333.05	0.0028
0.2500	353.15	0.0018
0.2500	384.95	0.0010
0.2500	396.75	0.0009
0.2500	413.25	0.0007
0.2500	430.35	0.0006
0.2500	445.65	0.0005
0.5000	293.45	0.0220
0.5000	312.95	0.0096
0.5000	332.95	0.0050
0.5000	352.95	0.0030
0.5000	382.55	0.0017
0.5000	394.25	0.0014
0.5000	409.35	0.0011
0.5000	428.25	0.0009
0.5000	447.05	0.0007
0.7500	294.05	0.0304
0.7500	313.05	0.0133
0.7500	333.05	0.0067
0.7500	353.05	0.0039
0.7500	385.05	0.0020
0.7500	394.95	0.0017
0.7500	410.95	0.0014
0.7500	428.65	0.0010
0.7500	447.65	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0008
303.15	0.0501	0.0016
303.15	0.1016	0.0026
303.15	0.1512	0.0038
303.15	0.2012	0.0053
303.15	0.2477	0.0067
303.15	0.2980	0.0083
303.15	0.3505	0.0099
303.15	0.4483	0.0125
303.15	0.5421	0.0151
303.15	0.6518	0.0175
303.15	0.7525	0.0193
303.15	0.7864	0.0199
303.15	0.8499	0.0206
303.15	0.9005	0.0213
303.15	0.9503	0.0217
303.15	1.0000	0.0222
308.15	0.0000	0.0007
308.15	0.0501	0.0014
308.15	0.1016	0.0022
308.15	0.1512	0.0033
308.15	0.2012	0.0044
308.15	0.2477	0.0056
308.15	0.2980	0.0069
308.15	0.3505	0.0082
308.15	0.4483	0.0103
308.15	0.5421	0.0123
308.15	0.6518	0.0141
308.15	0.7525	0.0156
308.15	0.7864	0.0161
308.15	0.8499	0.0167
308.15	0.9005	0.0172
308.15	0.9503	0.0175
308.15	1.0000	0.0179
313.15	0.0000	0.0007
313.15	0.0501	0.0012
313.15	0.1016	0.0020
313.15	0.1512	0.0028
313.15	0.2012	0.0038
313.15	0.2477	0.0047
313.15	0.2980	0.0058
313.15	0.3505	0.0068
313.15	0.4483	0.0085
313.15	0.5421	0.0101
313.15	0.6518	0.0116
313.15	0.7525	0.0128
313.15	0.7864	0.0132
313.15	0.8499	0.0137
313.15	0.9005	0.0141
313.15	0.9503	0.0144
313.15	1.0000	0.0147
318.15	0.0000	0.0006
318.15	0.0501	0.0011
318.15	0.1016	0.0017
318.15	0.1512	0.0025
318.15	0.2012	0.0033
318.15	0.2477	0.0041
318.15	0.2980	0.0050
318.15	0.3505	0.0058
318.15	0.4483	0.0071
318.15	0.5421	0.0085
318.15	0.6518	0.0097
318.15	0.7525	0.0106
318.15	0.7864	0.0110
318.15	0.8499	0.0114
318.15	0.9005	0.0117
318.15	0.9503	0.0119
318.15	1.0000	0.0122
323.15	0.0000	0.0005
323.15	0.0501	0.0010
323.15	0.1016	0.0015
323.15	0.1512	0.0022
323.15	0.2012	0.0028
323.15	0.2477	0.0035
323.15	0.2980	0.0043
323.15	0.3505	0.0049
323.15	0.4483	0.0061
323.15	0.5421	0.0071
323.15	0.6518	0.0081
323.15	0.7525	0.0089
323.15	0.7864	0.0092
323.15	0.8499	0.0095
323.15	0.9005	0.0098
323.15	0.9503	0.0100
323.15	1.0000	0.0102

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Water (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1026	-0.2750
0.2012	-0.5110
0.2094	-0.5210
0.3067	-0.7410
0.4068	-0.9310
0.4937	-1.039
0.5018	-1.066
0.6003	-1.192
0.6996	-1.245
0.7998	-1.172
0.8999	-0.8570
0.9002	-0.8670
0.9498	-0.5380

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2000	-1.219
0.4010	-1.217
0.5010	-1.149
0.8040	-0.4630

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
0.1100	1.4341
0.2000	1.4241
0.3000	1.4134
0.4100	1.4011
0.5000	1.3892
0.6000	1.3782
0.7000	1.3662
0.8000	1.3541
0.9000	1.3426
1.0000	1.3318

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0985	999.65
293.15	0.1974	1001.03
293.15	0.2950	1002.36
293.15	0.4101	1003.86
293.15	0.5006	1004.99
303.15	0.0985	997.07
303.15	0.1974	998.39
303.15	0.2950	999.64
303.15	0.4101	1001.05
303.15	0.5006	1002.15
293.15	0.0000	998.21
303.15	0.0000	995.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0097	1006.17
293.15	0.0201	1013.774
293.15	0.0297	1020.398
293.15	0.0397	1026.981
293.15	0.0502	1033.245
293.15	0.0591	1038.24
293.15	0.0703	1044.159
293.15	0.0796	1048.669
293.15	0.0897	1053.152
293.15	0.1004	1057.714
293.15	0.1507	1074.468
293.15	0.1996	1085.68
293.15	0.2467	1093.589
293.15	0.2943	1098.855
293.15	0.3511	1103.727
293.15	0.3995	1106.647
293.15	0.4527	1109.078
293.15	0.5008	1110.756
293.15	0.5449	1111.946
293.15	0.5834	1112.812
293.15	0.6482	1113.95
293.15	0.6982	1114.602
293.15	0.7444	1115.11
293.15	0.7962	1115.574
293.15	0.8401	1115.893
293.15	0.8947	1116.234
293.15	0.9092	1116.317
293.15	0.9190	1116.369
293.15	0.9303	1116.392
293.15	0.9393	1116.4
293.15	0.9473	1116.498
293.15	0.9566	1116.546
293.15	0.9694	1116.601
293.15	0.9801	1116.648
293.15	0.9915	1116.69
298.15	0.0097	1004.885
298.15	0.0201	1012.33
298.15	0.0297	1018.801
298.15	0.0397	1025.226
298.15	0.0502	1031.33
298.15	0.0591	1036.189
298.15	0.0703	1041.951
298.15	0.0796	1046.341
298.15	0.0897	1050.705
298.15	0.1004	1055.142
298.15	0.1507	1071.485
298.15	0.1996	1082.45
298.15	0.2467	1090.206
298.15	0.2943	1095.375
298.15	0.3511	1100.191
298.15	0.3995	1103.051
298.15	0.4527	1105.496
298.15	0.5008	1107.171
298.15	0.5449	1108.361
298.15	0.5834	1109.228
298.15	0.6482	1110.368
298.15	0.6982	1111.024
298.15	0.7444	1111.536
298.15	0.7962	1112.005
298.15	0.8401	1112.329
298.15	0.8947	1112.673
298.15	0.9092	1112.755
298.15	0.9190	1112.81
298.15	0.9303	1112.845
298.15	0.9393	1112.85
298.15	0.9473	1112.94
298.15	0.9566	1112.989
298.15	0.9694	1113.044
298.15	0.9801	1113.092
298.15	0.9915	1113.135
303.15	0.0097	1003.366
303.15	0.0201	1010.671
303.15	0.0297	1017.004
303.15	0.0397	1023.281
303.15	0.0502	1029.242
303.15	0.0591	1033.98
303.15	0.0703	1039.597
303.15	0.0796	1043.879
303.15	0.0897	1048.134
303.15	0.1004	1052.456
303.15	0.1507	1068.416
303.15	0.1996	1079.151
303.15	0.2467	1086.765
303.15	0.2943	1091.844
303.15	0.3511	1096.608
303.15	0.3995	1099.417
303.15	0.4527	1101.877
303.15	0.5008	1103.557
303.15	0.5449	1104.748
303.15	0.5834	1105.614
303.15	0.6482	1106.76
303.15	0.6982	1107.423
303.15	0.7444	1107.937
303.15	0.7962	1108.413
303.15	0.8401	1108.739
303.15	0.8947	1109.088
303.15	0.9092	1109.172
303.15	0.9190	1109.229
303.15	0.9303	1109.267
303.15	0.9393	1109.277
303.15	0.9473	1109.361
303.15	0.9566	1109.41
303.15	0.9694	1109.467
303.15	0.9801	1109.516
303.15	0.9915	1109.562
308.15	0.0097	1001.634
308.15	0.0201	1008.814
308.15	0.0297	1015.021
308.15	0.0397	1021.167
308.15	0.0502	1026.994
308.15	0.0591	1031.626
308.15	0.0703	1037.108
308.15	0.0796	1041.293
308.15	0.0897	1045.448
308.15	0.1004	1049.659
308.15	0.1507	1065.271
308.15	0.1996	1075.794
308.15	0.2467	1083.272
308.15	0.2943	1088.253
308.15	0.3511	1092.986
308.15	0.3995	1095.833
308.15	0.4527	1098.237
308.15	0.5008	1099.92
308.15	0.5449	1101.11
308.15	0.5834	1101.985
308.15	0.6482	1103.133
308.15	0.6982	1103.802
308.15	0.7444	1104.328
308.15	0.7962	1104.809
308.15	0.8401	1105.138
308.15	0.8947	1105.494
308.15	0.9092	1105.578
308.15	0.9190	1105.636
308.15	0.9303	1105.678
308.15	0.9393	1105.694
308.15	0.9473	1105.769
308.15	0.9566	1105.82
308.15	0.9694	1105.878
308.15	0.9801	1105.926
308.15	0.9915	1105.973
293.15	0.0000	998.429
298.15	0.0000	997.267
303.15	0.0000	995.867
308.15	0.0000	994.252
293.15	1.0000	1116.733
298.15	1.0000	1113.174
303.15	1.0000	1109.599
308.15	1.0000	1106.013
293.15	0.0490	1032.591
293.15	0.0992	1057.143
293.15	0.1490	1074.037
293.15	0.1998	1085.893
293.15	0.2490	1093.806
293.15	0.2987	1099.437
293.15	0.3501	1103.603
293.15	0.4007	1106.626
293.15	0.4504	1108.903
293.15	0.4973	1110.602
293.15	0.5530	1112.185
293.15	0.5938	1113.094
293.15	0.6514	1114.071
293.15	0.6864	1114.522
293.15	0.7556	1115.186
293.15	0.7999	1115.521
293.15	0.8525	1115.894
293.15	0.9002	1116.233
293.15	0.9554	1116.574
298.15	0.0490	1030.669
298.15	0.0992	1054.615
298.15	0.1490	1071.09
298.15	0.1998	1082.664
298.15	0.2490	1090.405
298.15	0.2987	1095.935
298.15	0.3501	1100.047
298.15	0.4007	1103.049
298.15	0.4504	1105.321
298.15	0.4973	1107.021
298.15	0.5530	1108.607
298.15	0.5938	1109.516
298.15	0.6514	1110.493
298.15	0.6864	1110.943
298.15	0.7556	1111.608
298.15	0.7999	1111.947
298.15	0.8525	1112.329
298.15	0.9002	1112.677
298.15	0.9554	1113.023
303.15	0.0490	1028.576
303.15	0.0992	1051.966
303.15	0.1490	1068.055
303.15	0.1998	1079.366
303.15	0.2490	1086.946
303.15	0.2987	1092.382
303.15	0.3501	1096.446
303.15	0.4007	1099.431
303.15	0.4504	1101.701
303.15	0.4973	1103.405
303.15	0.5530	1104.997
303.15	0.5938	1105.91
303.15	0.6514	1106.888
303.15	0.6864	1107.338
303.15	0.7556	1108.005
303.15	0.7999	1108.346
303.15	0.8525	1108.736
303.15	0.9002	1109.094
303.15	0.9554	1109.446
308.15	0.0490	1026.325
308.15	0.0992	1049.205
308.15	0.1490	1064.938
308.15	0.1998	1076.008
308.15	0.2490	1083.444
308.15	0.2987	1088.798
308.15	0.3501	1092.823
308.15	0.4007	1095.796
308.15	0.4504	1098.068
308.15	0.4973	1099.779
308.15	0.5530	1101.377
308.15	0.5938	1102.291
308.15	0.6514	1103.268
308.15	0.6864	1103.717
308.15	0.7556	1104.385
308.15	0.7999	1104.732
308.15	0.8525	1105.132
308.15	0.9002	1105.502
308.15	0.9554	1105.863

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0985	1000.689
288.15	0.1974	1002.06
288.15	0.2950	1003.358
288.15	0.4101	1004.837
288.15	0.5006	1005.961
288.15	0.6001	1007.125
288.15	0.6996	1008.278
288.15	0.7999	1009.393
298.15	0.0985	998.458
298.15	0.1974	999.78
298.15	0.2950	1001.026
298.15	0.4101	1002.49
298.15	0.5006	1003.585
298.15	0.6001	1004.735
298.15	0.6996	1005.827
298.15	0.7999	1006.873
308.15	0.0985	995.44
308.15	0.1974	996.778
308.15	0.2950	998.046
308.15	0.4101	999.471
308.15	0.5006	1000.531
308.15	0.6001	1001.676
308.15	0.6996	1002.761
308.15	0.7999	1003.829
318.15	0.0985	991.758
318.15	0.1974	993.102
318.15	0.2950	994.366
318.15	0.4101	995.788
318.15	0.5006	996.853
318.15	0.6001	997.974
318.15	0.6996	999.056
318.15	0.7999	1000.108

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0985	293.15	999.647
0.1974	293.15	1001.031
0.2950	293.15	1002.356
0.4101	293.15	1003.859
0.5006	293.15	1004.993
0.0985	298.15	998.458
0.1974	298.15	999.78
0.2950	298.15	1001.026
0.4101	298.15	1002.49
0.5006	298.15	1003.585
0.0985	303.15	997.071
0.1974	303.15	998.395
0.2950	303.15	999.643
0.4101	303.15	1001.051
0.5006	303.15	1002.146
0.0985	308.15	995.44
0.1974	308.15	996.778
0.2950	308.15	998.046
0.4101	308.15	999.471
0.5006	308.15	1000.531

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	999.7
283.15	0.0255	1019.73
283.15	0.0565	1040.15
283.15	0.1027	1063.34
283.15	0.1966	1091.18
283.15	0.3010	1106.34
283.15	0.3989	1113.62
283.15	0.5006	1117.88
283.15	0.6011	1120.39
283.15	0.7003	1121.98
283.15	0.8051	1123.07
283.15	0.8920	1123.64
283.15	1.0000	1124.24
288.15	0.0000	999.1
288.15	0.0255	1018.61
288.15	0.0565	1038.42
288.15	0.1027	1060.91
288.15	0.1966	1088.01
288.15	0.3010	1102.88
288.15	0.3989	1110.06
288.15	0.5006	1114.29
288.15	0.6011	1116.8
288.15	0.7003	1118.39
288.15	0.8051	1119.47
288.15	0.8920	1120.05
288.15	1.0000	1120.65
293.15	0.0000	998.2
293.15	0.0255	1017.27
293.15	0.0565	1036.53
293.15	0.1027	1058.39
293.15	0.1966	1084.81
293.15	0.3010	1099.4
293.15	0.3989	1106.48
293.15	0.5006	1110.68
293.15	0.6011	1113.19
293.15	0.7003	1114.79
293.15	0.8051	1115.87
293.15	0.8920	1116.45
293.15	1.0000	1117.05
298.15	0.0000	997.04
298.15	0.0255	1015.72
298.15	0.0565	1034.5
298.15	0.1027	1055.77
298.15	0.1966	1081.56
298.15	0.3010	1095.89
298.15	0.3989	1102.89
298.15	0.5006	1107.07
298.15	0.6011	1109.59
298.15	0.7003	1111.19
298.15	0.8051	1112.27
298.15	0.8920	1112.86
298.15	1.0000	1113.47
303.15	0.0000	995.55
303.15	0.0255	1013.97
303.15	0.0565	1032.33
303.15	0.1027	1053.07
303.15	0.1966	1078.28
303.15	0.3010	1092.36
303.15	0.3989	1099.29
303.15	0.5006	1103.45
303.15	0.6011	1105.97
303.15	0.7003	1107.58
303.15	0.8051	1108.67
303.15	0.8920	1109.27
303.15	1.0000	1109.88
308.15	0.0000	994.03
308.15	0.0255	1011.83
308.15	0.0565	1030.02
308.15	0.1027	1050.27
308.15	0.1966	1074.94
308.15	0.3010	1088.8
308.15	0.3989	1095.67
308.15	0.5006	1099.82
308.15	0.6011	1102.36
308.15	0.7003	1103.97
308.15	0.8051	1105.06
308.15	0.8920	1105.68
308.15	1.0000	1106.29
313.15	0.0000	992.21
313.15	0.0255	1009.99
313.15	0.0565	1027.57
313.15	0.1027	1047.39
313.15	0.1966	1071.56
313.15	0.3010	1085.22
313.15	0.3989	1092.03
313.15	0.5006	1096.18
313.15	0.6011	1098.73
313.15	0.7003	1100.35
313.15	0.8051	1101.45
313.15	0.8920	1102.09
313.15	1.0000	1102.7
318.15	0.0000	990.21
318.15	0.0255	1007.73
318.15	0.0565	1025.01
318.15	0.1027	1044.41
318.15	0.1966	1068.13
318.15	0.3010	1081.61
318.15	0.3989	1088.37
318.15	0.5006	1092.53
318.15	0.6011	1095.08
318.15	0.7003	1096.71
318.15	0.8051	1097.83
318.15	0.8920	1098.49
318.15	1.0000	1099.11
323.15	0.0000	988.03
323.15	0.0255	1005.37
323.15	0.0565	1022.33
323.15	0.1027	1041.36
323.15	0.1966	1064.65
323.15	0.3010	1077.97
323.15	0.3989	1084.69
323.15	0.5006	1088.85
323.15	0.6011	1091.42
323.15	0.7003	1093.07
323.15	0.8051	1094.21
323.15	0.8920	1094.88
323.15	1.0000	1095.51
328.15	0.0000	985.69
328.15	0.0255	1002.86
328.15	0.0565	1019.53
328.15	0.1027	1038.21
328.15	0.1966	1061.13
328.15	0.3010	1074.29
328.15	0.3989	1080.98
328.15	0.5006	1085.16
328.15	0.6011	1087.74
328.15	0.7003	1089.41
328.15	0.8051	1090.57
328.15	0.8920	1091.26
328.15	1.0000	1091.91
333.15	0.0000	983.19
333.15	0.0255	1000.22
333.15	0.0565	1016.62
333.15	0.1027	1034.99
333.15	0.1966	1057.55
333.15	0.3010	1070.58
333.15	0.3989	1077.25
333.15	0.5006	1081.43
333.15	0.6011	1084.04
333.15	0.7003	1085.74
333.15	0.8051	1086.93
333.15	0.8920	1087.63
333.15	1.0000	1088.3
338.15	0.0000	980.55
338.15	0.0255	997.46
338.15	0.0565	1013.61
338.15	0.1027	1031.68
338.15	0.1966	1053.92
338.15	0.3010	1066.84
338.15	0.3989	1073.49
338.15	0.5006	1077.69
338.15	0.6011	1080.33
338.15	0.7003	1082.06
338.15	0.8051	1083.27
338.15	0.8920	1083.99
338.15	1.0000	1084.68
343.15	0.0000	977.76
343.15	0.0255	994.57
343.15	0.0565	1010.51
343.15	0.1027	1028.29
343.15	0.1966	1050.24
343.15	0.3010	1063.06
343.15	0.3989	1069.69
343.15	0.5006	1073.93
343.15	0.6011	1076.59
343.15	0.7003	1078.36
343.15	0.8051	1079.6
343.15	0.8920	1080.34
343.15	1.0000	1081.05
348.15	0.0000	974.84
348.15	0.0255	991.57
348.15	0.0565	1007.27
348.15	0.1027	1024.84
348.15	0.1966	1046.51
348.15	0.3010	1059.24
348.15	0.3989	1065.88
348.15	0.5006	1070.14
348.15	0.6011	1072.84
348.15	0.7003	1074.63
348.15	0.8051	1075.91
348.15	0.8920	1076.67
348.15	1.0000	1077.4
353.15	0.0000	971.79
353.15	0.0255	988.5
353.15	0.0565	1004.07
353.15	0.1027	1021.3
353.15	0.1966	1042.72
353.15	0.3010	1055.38
353.15	0.3989	1062.02
353.15	0.5006	1066.32
353.15	0.6011	1069.05
353.15	0.7003	1070.89
353.15	0.8051	1072.2
353.15	0.8920	1072.99
353.15	1.0000	1073.74

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.9070	1123.135
288.15	0.9070	1119.575
293.15	0.9070	1116.018
298.15	0.9070	1112.454
303.15	0.9070	1108.881
308.15	0.9070	1105.295
313.15	0.9070	1101.695
323.15	0.9070	1094.447
333.15	0.9070	1087.119
343.15	0.9070	1079.71
283.15	0.9589	1123.266
288.15	0.9589	1119.71
293.15	0.9589	1116.151
298.15	0.9589	1112.585
303.15	0.9589	1109.016
308.15	0.9589	1105.431
313.15	0.9589	1101.834
323.15	0.9589	1094.595
333.15	0.9589	1087.278
343.15	0.9589	1079.883
283.15	0.9698	1123.273
288.15	0.9698	1119.716
293.15	0.9698	1116.159
298.15	0.9698	1112.594
303.15	0.9698	1109.025
308.15	0.9698	1105.442
313.15	0.9698	1101.843
323.15	0.9698	1094.603
333.15	0.9698	1087.288
343.15	0.9698	1079.897
283.15	0.9900	1123.325
288.15	0.9900	1119.767
293.15	0.9900	1116.211
298.15	0.9900	1112.649
303.15	0.9900	1109.077
308.15	0.9900	1105.496
313.15	0.9900	1101.9
323.15	0.9900	1094.667
333.15	0.9900	1087.359
343.15	0.9900	1079.973
283.15	0.9901	1123.327
288.15	0.9901	1119.771
293.15	0.9901	1116.213
298.15	0.9901	1112.651
303.15	0.9901	1109.081
308.15	0.9901	1105.498
313.15	0.9901	1101.903
323.15	0.9901	1094.668
333.15	0.9901	1087.356
343.15	0.9901	1079.969

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.2500	294.25	1095.0
0.2500	313.05	1081.0
0.2500	333.05	1066.0
0.2500	353.15	1051.0
0.2500	381.45	1027.0
0.2500	392.75	1017.0
0.2500	409.25	1004.0
0.2500	426.35	987.6
0.2500	441.65	973.3
0.5000	293.45	1111.0
0.5000	312.95	1097.0
0.5000	332.95	1082.0
0.5000	352.95	1066.0
0.5000	380.05	1043.0
0.5000	390.25	1035.0
0.5000	405.35	1023.0
0.5000	424.25	1006.0
0.5000	443.05	988.2
0.7500	294.05	1115.0
0.7500	313.05	1101.0
0.7500	333.05	1087.0
0.7500	353.05	1071.0
0.7500	382.55	1048.0
0.7500	390.95	1042.0
0.7500	406.95	1029.0
0.7500	424.65	1014.0
0.7500	443.65	996.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0511	1000.743
278.15	0.1025	1001.52
278.15	0.2049	1003.056
278.15	0.2972	1004.427
278.15	0.4063	1006.029
283.15	0.0511	1000.462
283.15	0.1025	1001.222
283.15	0.2049	1002.721
283.15	0.2972	1004.058
283.15	0.4063	1005.619
288.15	0.0511	999.849
288.15	0.1025	1000.593
288.15	0.2049	1002.061
288.15	0.2972	1003.369
288.15	0.4063	1004.895
293.15	0.0511	998.941
293.15	0.1025	999.67
293.15	0.2049	1001.113
293.15	0.2972	1002.394
293.15	0.4063	1003.891
298.15	0.0511	997.772
298.15	0.1025	998.489
298.15	0.2049	999.907
298.15	0.2972	1001.167
298.15	0.4063	1002.636
303.15	0.0511	996.365
303.15	0.1025	997.071
303.15	0.2049	998.466
303.15	0.2972	999.707
303.15	0.4063	1001.152
308.15	0.0511	994.74
308.15	0.1025	995.437
308.15	0.2049	996.813
308.15	0.2972	998.034
308.15	0.4063	999.457
313.15	0.0511	992.916
313.15	0.1025	993.604
313.15	0.2049	994.96
313.15	0.2972	996.164
313.15	0.4063	997.567
318.15	0.0511	990.905
318.15	0.1025	991.585
318.15	0.2049	992.924
318.15	0.2972	994.112
318.15	0.4063	995.495
323.15	0.0511	988.72
323.15	0.1025	989.393
323.15	0.2049	990.716
323.15	0.2972	991.889
323.15	0.4063	993.254
328.15	0.0511	986.371
328.15	0.1025	987.036
328.15	0.2049	988.343
328.15	0.2972	989.503
328.15	0.4063	990.852
333.15	0.0511	983.864
333.15	0.1025	984.525
333.15	0.2049	985.817
333.15	0.2972	986.963
333.15	0.4063	988.296
338.15	0.0511	981.213
338.15	0.1025	981.866
338.15	0.2049	983.145
338.15	0.2972	984.279
338.15	0.4063	985.595
343.15	0.0511	978.42
343.15	0.1025	979.067
343.15	0.2049	980.331
343.15	0.2972	981.454
343.15	0.4063	982.755

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	995.6
303.15	0.0501	1028.38
303.15	0.1016	1051.83
303.15	0.1512	1067.99
303.15	0.2012	1078.71
303.15	0.2477	1086.55
303.15	0.2980	1092.27
303.15	0.3505	1096.22
303.15	0.4483	1101.17
303.15	0.5421	1103.74
303.15	0.6518	1106.25
303.15	0.7525	1107.78
303.15	0.7864	1107.94
303.15	0.8499	1108.55
303.15	0.9005	1108.84
303.15	0.9503	1109.66
303.15	1.0000	1109.48
308.15	0.0000	994.12
308.15	0.0501	1026.09
308.15	0.1016	1048.94
308.15	0.1512	1065.34
308.15	0.2012	1075.25
308.15	0.2477	1082.95
308.15	0.2980	1088.52
308.15	0.3505	1092.42
308.15	0.4483	1097.58
308.15	0.5421	1100.11
308.15	0.6518	1102.58
308.15	0.7525	1103.95
308.15	0.7864	1104.26
308.15	0.8499	1104.93
308.15	0.9005	1105.16
308.15	0.9503	1105.58
308.15	1.0000	1105.72
313.15	0.0000	992.25
313.15	0.0501	1023.67
313.15	0.1016	1046.02
313.15	0.1512	1062.04
313.15	0.2012	1071.77
313.15	0.2477	1079.42
313.15	0.2980	1084.97
313.15	0.3505	1088.68
313.15	0.4483	1093.68
313.15	0.5421	1096.37
313.15	0.6518	1098.97
313.15	0.7525	1100.25
313.15	0.7864	1100.56
313.15	0.8499	1101.32
313.15	0.9005	1101.55
313.15	0.9503	1101.98
313.15	1.0000	1102.11
318.15	0.0000	990.3
318.15	0.0501	1021.08
318.15	0.1016	1043.03
318.15	0.1512	1058.72
318.15	0.2012	1068.24
318.15	0.2477	1075.76
318.15	0.2980	1081.58
318.15	0.3505	1084.97
318.15	0.4483	1089.91
318.15	0.5421	1092.91
318.15	0.6518	1095.29
318.15	0.7525	1096.58
318.15	0.7864	1096.89
318.15	0.8499	1097.62
318.15	0.9005	1097.87
318.15	0.9503	1098.33
318.15	1.0000	1098.35
323.15	0.0000	988.1
323.15	0.0501	1018.36
323.15	0.1016	1039.94
323.15	0.1512	1055.2
323.15	0.2012	1064.5
323.15	0.2477	1072.18
323.15	0.2980	1077.47
323.15	0.3505	1081.16
323.15	0.4483	1086.1
323.15	0.5421	1088.98
323.15	0.6518	1091.34
323.15	0.7525	1093.18
323.15	0.7864	1093.37
323.15	0.8499	1093.91
323.15	0.9005	1094.19
323.15	0.9503	1094.55
323.15	1.0000	1094.94

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0985	1487.7
293.15	0.1974	1493.1
293.15	0.2950	1498.1
293.15	0.4101	1504.1
293.15	0.5006	1508.3
303.15	0.0985	1513.1
303.15	0.1974	1517.6
303.15	0.2950	1522.0
303.15	0.4101	1526.9
303.15	0.5006	1530.6
293.15	0.0000	1482.3
303.15	0.0000	1508.5

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 92.3 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0097	1511.15
293.15	0.0201	1539.56
293.15	0.0297	1563.59
293.15	0.0397	1586.15
293.15	0.0502	1607.67
293.15	0.0591	1623.95
293.15	0.0703	1642.55
293.15	0.0796	1655.49
293.15	0.0897	1667.88
293.15	0.1004	1679.66
293.15	0.1507	1713.04
293.15	0.1996	1723.89
293.15	0.2467	1723.01
293.15	0.2943	1716.57
293.15	0.3511	1705.08
293.15	0.3995	1694.05
293.15	0.4527	1681.69
293.15	0.5008	1670.71
293.15	0.5449	1661.45
293.15	0.5834	1653.41
293.15	0.6482	1640.67
293.15	0.6982	1632.2
293.15	0.7444	1624.39
293.15	0.7962	1616.66
293.15	0.8401	1610.38
293.15	0.8947	1603.32
293.15	0.9092	1601.45
293.15	0.9190	1600.23
293.15	0.9303	1599.06
293.15	0.9393	1598.01
293.15	0.9473	1597.15
293.15	0.9566	1595.98
293.15	0.9694	1594.59
293.15	0.9801	1593.4
293.15	0.9915	1592.14
298.15	0.0097	1522.97
298.15	0.0201	1549.09
298.15	0.0297	1571.11
298.15	0.0397	1591.7
298.15	0.0502	1611.33
298.15	0.0591	1626.12
298.15	0.0703	1643.04
298.15	0.0796	1654.71
298.15	0.0897	1665.88
298.15	0.1004	1676.48
298.15	0.1507	1705.92
298.15	0.1996	1714.67
298.15	0.2467	1712.57
298.15	0.2943	1705.45
298.15	0.3511	1693.48
298.15	0.3995	1682.2
298.15	0.4527	1669.76
298.15	0.5008	1658.74
298.15	0.5449	1649.42
298.15	0.5834	1641.4
298.15	0.6482	1628.68
298.15	0.6982	1620.25
298.15	0.7444	1612.47
298.15	0.7962	1604.75
298.15	0.8401	1598.51
298.15	0.8947	1591.46
298.15	0.9092	1589.6
298.15	0.9190	1588.38
298.15	0.9303	1587.24
298.15	0.9393	1586.16
298.15	0.9473	1585.29
298.15	0.9566	1584.12
298.15	0.9694	1582.74
298.15	0.9801	1581.55
298.15	0.9915	1580.29
303.15	0.0097	1533.23
303.15	0.0201	1557.23
303.15	0.0297	1577.38
303.15	0.0397	1596.13
303.15	0.0502	1614.02
303.15	0.0591	1627.38
303.15	0.0703	1642.71
303.15	0.0796	1653.19
303.15	0.0897	1663.2
303.15	0.1004	1672.68
303.15	0.1507	1698.47
303.15	0.1996	1705.09
303.15	0.2467	1701.82
303.15	0.2943	1694.07
303.15	0.3511	1681.7
303.15	0.3995	1670.2
303.15	0.4527	1657.65
303.15	0.5008	1646.57
303.15	0.5449	1637.26
303.15	0.5834	1629.22
303.15	0.6482	1616.58
303.15	0.6982	1608.12
303.15	0.7444	1600.43
303.15	0.7962	1592.72
303.15	0.8401	1586.58
303.15	0.8947	1579.52
303.15	0.9092	1577.65
303.15	0.9190	1576.47
303.15	0.9303	1575.31
303.15	0.9393	1574.27
303.15	0.9473	1573.35
303.15	0.9566	1572.17
303.15	0.9694	1570.82
303.15	0.9801	1569.62
303.15	0.9915	1568.35
308.15	0.0097	1541.96
308.15	0.0201	1563.99
308.15	0.0297	1582.41
308.15	0.0397	1599.44
308.15	0.0502	1615.66
308.15	0.0591	1627.75
308.15	0.0703	1641.6
308.15	0.0796	1650.94
308.15	0.0897	1659.89
308.15	0.1004	1668.31
308.15	0.1507	1690.55
308.15	0.1996	1695.23
308.15	0.2467	1690.86
308.15	0.2943	1682.5
308.15	0.3511	1669.71
308.15	0.3995	1658.05
308.15	0.4527	1645.42
308.15	0.5008	1634.33
308.15	0.5449	1625.03
308.15	0.5834	1617.03
308.15	0.6482	1604.4
308.15	0.6982	1596.02
308.15	0.7444	1588.33
308.15	0.7962	1580.66
308.15	0.8401	1574.51
308.15	0.8947	1567.53
308.15	0.9092	1565.66
308.15	0.9190	1564.48
308.15	0.9303	1563.32
308.15	0.9393	1562.29
308.15	0.9473	1561.39
308.15	0.9566	1560.2
308.15	0.9694	1558.86
308.15	0.9801	1557.66
308.15	0.9915	1556.4
293.15	0.0000	1482.78
298.15	0.0000	1496.99
303.15	0.0000	1509.32
308.15	0.0000	1519.89
293.15	1.0000	1591.03
298.15	1.0000	1579.13
303.15	1.0000	1567.21
308.15	1.0000	1555.26

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0985	1472.11
288.15	0.1974	1478.01
288.15	0.2950	1483.78
288.15	0.4101	1489.36
288.15	0.5006	1494.73
288.15	0.6001	1500.28
288.15	0.6996	1505.69
288.15	0.7999	1510.78
298.15	0.0985	1501.24
298.15	0.1974	1506.01
298.15	0.2950	1510.78
298.15	0.4101	1516.15
298.15	0.5006	1520.34
298.15	0.6001	1527.06
298.15	0.6996	1534.55
298.15	0.7999	1540.32
308.15	0.0985	1523.52
308.15	0.1974	1527.52
308.15	0.2950	1531.47
308.15	0.4101	1536.11
308.15	0.5006	1541.59
308.15	0.6001	1549.18
308.15	0.6996	1556.59
308.15	0.7999	1562.29
318.15	0.0985	1541.59
318.15	0.1974	1547.17
318.15	0.2950	1552.68
318.15	0.4101	1558.07
318.15	0.5006	1563.21
318.15	0.6001	1568.76
318.15	0.6996	1573.92
318.15	0.7999	1579.48

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0985	293.15	1487.65
0.1974	293.15	1493.09
0.2950	293.15	1498.14
0.4101	293.15	1504.13
0.5006	293.15	1508.33
0.0985	298.15	1501.24
0.1974	298.15	1506.01
0.2950	298.15	1510.78
0.4101	298.15	1516.15
0.5006	298.15	1520.34
0.0985	303.15	1513.09
0.1974	303.15	1517.58
0.2950	303.15	1521.95
0.4101	303.15	1526.88
0.5006	303.15	1530.64
0.0985	308.15	1523.52
0.1974	308.15	1527.52
0.2950	308.15	1531.47
0.4101	308.15	1536.11
0.5006	308.15	1539.59

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.9070	1620.3
288.15	0.9070	1608.0
293.15	0.9070	1595.9
298.15	0.9070	1583.8
303.15	0.9070	1571.7
308.15	0.9070	1559.6
313.15	0.9070	1547.5
323.15	0.9070	1523.4
333.15	0.9070	1499.0
343.15	0.9070	1474.6
283.15	0.9589	1617.8
288.15	0.9589	1605.5
293.15	0.9589	1593.3
298.15	0.9589	1581.0
303.15	0.9589	1569.0
308.15	0.9589	1557.0
313.15	0.9589	1545.0
323.15	0.9589	1520.9
333.15	0.9589	1496.6
343.15	0.9589	1472.2
283.15	0.9698	1617.4
288.15	0.9698	1605.2
293.15	0.9698	1593.0
298.15	0.9698	1580.8
303.15	0.9698	1568.6
308.15	0.9698	1556.6
313.15	0.9698	1544.6
323.15	0.9698	1520.5
333.15	0.9698	1496.2
343.15	0.9698	1471.8
283.15	0.9900	1616.4
288.15	0.9900	1604.1
293.15	0.9900	1591.9
298.15	0.9900	1579.6
303.15	0.9900	1567.5
308.15	0.9900	1555.4
313.15	0.9900	1543.4
323.15	0.9900	1519.3
333.15	0.9900	1495.1
343.15	0.9900	1470.8
283.15	0.9901	1616.5
288.15	0.9901	1604.2
293.15	0.9901	1592.0
298.15	0.9901	1579.8
303.15	0.9901	1567.4
308.15	0.9901	1555.4
313.15	0.9901	1543.3
323.15	0.9901	1519.2
333.15	0.9901	1494.9
343.15	0.9901	1470.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid	Speed of sound, m/s - Liquid
278.15	0.0511	1430.06
278.15	0.1025	1433.67
278.15	0.2049	1440.62
278.15	0.2972	1446.92
278.15	0.4063	1454.36
283.15	0.0511	1450.72
283.15	0.1025	1454.05
283.15	0.2049	1460.39
283.15	0.2972	1466.18
283.15	0.4063	1472.97
288.15	0.0511	1469.07
288.15	0.1025	1472.12
288.15	0.2049	1478.02
288.15	0.2972	1483.3
288.15	0.4063	1489.53
293.15	0.0511	1485.2
293.15	0.1025	1488.04
293.15	0.2049	1493.47
293.15	0.2972	1498.43
293.15	0.4063	1504.05
298.15	0.0511	1499.38
298.15	0.1025	1501.98
298.15	0.2049	1507.01
298.15	0.2972	1511.53
298.15	0.4063	1516.73
303.15	0.0511	1511.66
303.15	0.1025	1514.06
303.15	0.2049	1518.71
303.15	0.2972	1522.85
303.15	0.4063	1527.63
308.15	0.0511	1522.21
308.15	0.1025	1524.41
308.15	0.2049	1528.68
308.15	0.2972	1532.49
308.15	0.4063	1536.91
313.15	0.0511	1531.13
313.15	0.1025	1533.15
313.15	0.2049	1537.1
313.15	0.2972	1540.62
313.15	0.4063	1544.69
318.15	0.0511	1538.56
318.15	0.1025	1540.43
318.15	0.2049	1544.07
318.15	0.2972	1547.3
318.15	0.4063	1551.01
323.15	0.0511	1544.58
323.15	0.1025	1546.3
323.15	0.2049	1549.63
323.15	0.2972	1552.58
323.15	0.4063	1555.99
328.15	0.0511	1549.27
328.15	0.1025	1550.84
328.15	0.2049	1553.89
328.15	0.2972	1556.58
328.15	0.4063	1559.7
333.15	0.0511	1552.73
333.15	0.1025	1554.17
333.15	0.2049	1556.94
333.15	0.2972	1559.4
333.15	0.4063	1562.24
338.15	0.0511	1555.04
338.15	0.1025	1556.35
338.15	0.2049	1558.86
338.15	0.2972	1561.09
338.15	0.4063	1563.66
343.15	0.0511	1556.26
343.15	0.1025	1557.44
343.15	0.2049	1559.73
343.15	0.2972	1561.73
343.15	0.4063	1564.05

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
100.00	0.9980	372.60
100.00	0.9890	373.20
100.00	0.9790	373.72
100.00	0.9610	375.15
100.00	0.9180	376.19
100.00	0.8900	376.71
100.00	0.8560	377.17
100.00	0.7990	380.14
100.00	0.7750	381.31
100.00	0.7590	382.40
100.00	0.7110	383.93
100.00	0.6960	383.68
100.00	0.6580	385.91
100.00	0.6440	387.39
100.00	0.5620	393.37
100.00	0.4890	398.40
100.00	0.3850	409.60
100.00	0.3210	419.09
100.00	0.2460	429.60
70.00	0.9980	362.52
70.00	0.9800	363.73
70.00	0.9510	364.82
70.00	0.9110	365.91
70.00	0.8740	368.25
70.00	0.8740	367.05
70.00	0.7940	369.95
70.00	0.7190	372.60
70.00	0.6830	374.37
70.00	0.6610	376.34
70.00	0.6600	375.52
70.00	0.6140	377.37
70.00	0.5890	379.09
70.00	0.4960	385.08
70.00	0.3560	397.65
70.00	0.3180	402.77
70.00	0.2590	413.67
70.00	0.1900	424.56
50.00	0.9980	353.64
50.00	0.9640	355.40
50.00	0.9330	356.25
50.00	0.8900	358.15
50.00	0.8630	359.28
50.00	0.7930	362.15
50.00	0.6830	364.95
50.00	0.6570	366.30
50.00	0.6270	367.64
50.00	0.6270	367.64
50.00	0.6090	368.57
50.00	0.5110	374.35
50.00	0.4550	378.72
50.00	0.3630	387.50
50.00	0.3050	395.36
50.00	0.2390	403.18
50.00	0.2270	405.63

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
0.2500	294.40	0.2910
0.2500	323.40	0.3100
0.2500	347.40	0.3150
0.2500	373.00	0.3220
0.2500	396.00	0.3250
0.2500	421.50	0.3300
0.2500	447.50	0.3280
0.5000	295.90	0.2350
0.5000	322.10	0.2440
0.5000	347.80	0.2490
0.5000	371.90	0.2580
0.5000	395.60	0.2570
0.5000	422.00	0.2560
0.5000	447.00	0.2530
0.7500	296.40	0.2090
0.7500	323.80	0.2130
0.7500	349.60	0.2170
0.7500	373.20	0.2190
0.7500	396.90	0.2170
0.7500	421.60	0.2220
0.7500	446.80	0.2130

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
303.20	0.0000
308.20	0.0000
313.20	0.0000
318.20	0.0000
323.20	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid	Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.2000	303.20	0.0000
0.2000	308.20	0.0000
0.2000	313.20	0.0000
0.2000	318.20	0.0000
0.2000	323.20	0.0000
0.4000	303.20	0.0000
0.4000	308.20	0.0000
0.4000	313.20	0.0000
0.4000	318.20	0.0000
0.4000	323.20	0.0000
0.6000	303.20	0.0000
0.6000	308.20	0.0000
0.6000	313.20	0.0000
0.6000	318.20	0.0000
0.6000	323.20	0.0000
0.8000	303.20	0.0000
0.8000	308.20	0.0000
0.8000	313.20	0.0000
0.8000	318.20	0.0000
0.8000	323.20	0.0000

Sources

• Mutual diffusion coefficients of aqueous solutions of some glycols
• Liquid-liquid equilibrium in binary and ternary mixtures containing formaldehyde, water, methanol, methylal, and poly(oxymethylene) dimethyl ethers
• Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
• 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
• Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
• Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
• 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
• Investigation on Temperature-Dependent Volumetric and Acoustical Properties of Homologous Series of Glycols in Aqueous Sorbitol Solutions
• Measurement and Modeling of Isobaric Vapor-Liquid Equilibrium of Water + Glycols
• Thermodynamic Interactions Study of Some Ethylene Glycols in Aqueous Aniline Solutions at Different Temperatures: An Acoustical and Volumetric Approach
• Salting Effect of Sodium Hydroxide and Sodium Formate on the Liquid-Liquid Equilibrium of Polyoxymethylene Dimethyl Ethers in Aqueous Solution
• Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
• Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
• 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
• Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K

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