Mixture of Triethylene glycol + Water

Datasets

1. Mole fraction (2)
2. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
3. η - Viscosity, Pa*s (6)
4. Excess molar enthalpy (molar enthalpy (2)
5. μ_JT - Joule-Thomson coefficient, K/kPa (2)
6. n₀ - Refractive index (Na D-line) (2)
7. ρ_l - Mass density, kg/m3 (16)
8. c_sound,fluid - Speed of Sound, m/s (12)
9. T_boil - Boiling temperature at pressure P, K (4)
10. λ - Thermal conductivity, W/m/K (2)
11. Binary diffusion coefficient, m2/s (4)

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
0.1170	0.9829
0.1400	0.9780
0.1610	0.9833
0.1760	0.9908
0.1820	0.9872
0.2420	0.9930
0.2510	0.9945
0.3250	0.9965
0.3730	0.9978
0.4100	0.9980
0.5430	0.9992
0.7040	0.9997
0.7810	0.9998
0.8260	0.9998
0.8560	0.9999
0.8770	0.9999
0.8930	0.9999
0.9150	0.9999

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
0.1170	0.9829
0.1400	0.9780
0.1610	0.9833
0.1760	0.9908
0.1820	0.9872
0.2420	0.9930
0.2510	0.9945
0.3250	0.9965
0.3730	0.9978
0.4100	0.9980
0.5430	0.9992
0.7040	0.9997
0.7810	0.9998
0.8260	0.9998
0.8560	0.9999
0.8770	0.9999
0.8930	0.9999
0.9150	0.9999

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.2000	303.15	129.30
0.2000	313.15	131.00
0.2000	323.15	132.90
0.2000	333.15	135.10
0.2000	343.15	137.20
0.2000	353.15	139.70
0.4000	303.15	184.10
0.4000	313.15	186.30
0.4000	323.15	189.00
0.4000	333.15	192.10
0.4000	343.15	195.20
0.4000	353.15	198.70
0.5000	303.15	211.30
0.5000	313.15	213.60
0.5000	323.15	216.50
0.5000	333.15	219.80
0.5000	343.15	223.40
0.5000	353.15	227.30
0.6000	303.15	237.80
0.6000	313.15	240.50
0.6000	323.15	243.70
0.6000	333.15	249.70
0.6000	343.15	251.80
0.6000	353.15	256.10
0.8000	303.15	288.30
0.8000	313.15	291.80
0.8000	323.15	295.70
0.8000	333.15	300.30
0.8000	343.15	306.00
0.8000	353.15	311.30

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.2000	303.15	129.30
0.2000	313.15	131.00
0.2000	323.15	132.90
0.2000	333.15	135.10
0.2000	343.15	137.20
0.2000	353.15	139.70
0.4000	303.15	184.10
0.4000	313.15	186.30
0.4000	323.15	189.00
0.4000	333.15	192.10
0.4000	343.15	195.20
0.4000	353.15	198.70
0.5000	303.15	211.30
0.5000	313.15	213.60
0.5000	323.15	216.50
0.5000	333.15	219.80
0.5000	343.15	223.40
0.5000	353.15	227.30
0.6000	303.15	237.80
0.6000	313.15	240.50
0.6000	323.15	243.70
0.6000	333.15	249.70
0.6000	343.15	251.80
0.6000	353.15	256.10
0.8000	303.15	288.30
0.8000	313.15	291.80
0.8000	323.15	295.70
0.8000	333.15	300.30
0.8000	343.15	306.00
0.8000	353.15	311.30

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0250	0.0019
293.15	0.0489	0.0029
293.15	0.0754	0.0044
293.15	0.0993	0.0060
293.15	0.1500	0.0102
293.15	0.1993	0.0145
293.15	0.2526	0.0194
293.15	0.2998	0.0236
293.15	0.3539	0.0278
293.15	0.4009	0.0312
293.15	0.4492	0.0341
293.15	0.4992	0.0367
293.15	0.5484	0.0388
293.15	0.5996	0.0406
293.15	0.6506	0.0421
293.15	0.7010	0.0437
293.15	0.7567	0.0449
293.15	0.8035	0.0457
293.15	0.8406	0.0464
293.15	0.8981	0.0470
293.15	0.9489	0.0476
298.15	0.0250	0.0015
298.15	0.0489	0.0023
298.15	0.0754	0.0035
298.15	0.0993	0.0047
298.15	0.1500	0.0078
298.15	0.1993	0.0112
298.15	0.2526	0.0149
298.15	0.2998	0.0181
298.15	0.3539	0.0213
298.15	0.4009	0.0238
298.15	0.4492	0.0261
298.15	0.4992	0.0280
298.15	0.5484	0.0297
298.15	0.5996	0.0311
298.15	0.6506	0.0322
298.15	0.7010	0.0333
298.15	0.7567	0.0343
298.15	0.8035	0.0350
298.15	0.8406	0.0355
298.15	0.8981	0.0359
298.15	0.9489	0.0365
303.15	0.0250	0.0014
303.15	0.0489	0.0021
303.15	0.0754	0.0031
303.15	0.0993	0.0041
303.15	0.1500	0.0067
303.15	0.1993	0.0095
303.15	0.2526	0.0124
303.15	0.2998	0.0149
303.15	0.3539	0.0174
303.15	0.4009	0.0193
303.15	0.4492	0.0211
303.15	0.4992	0.0226
303.15	0.5484	0.0239
303.15	0.5996	0.0250
303.15	0.6506	0.0259
303.15	0.7010	0.0268
303.15	0.7567	0.0275
303.15	0.8035	0.0281
303.15	0.8406	0.0285
303.15	0.8981	0.0289
303.15	0.9489	0.0293
308.15	0.0250	0.0013
308.15	0.0489	0.0019
308.15	0.0754	0.0027
308.15	0.0993	0.0036
308.15	0.1500	0.0056
308.15	0.1993	0.0080
308.15	0.2526	0.0103
308.15	0.2998	0.0123
308.15	0.3539	0.0142
308.15	0.4009	0.0157
308.15	0.4492	0.0170
308.15	0.4992	0.0182
308.15	0.5484	0.0192
308.15	0.5996	0.0201
308.15	0.6506	0.0208
308.15	0.7010	0.0215
308.15	0.7567	0.0221
308.15	0.8035	0.0225
308.15	0.8406	0.0228
308.15	0.8981	0.0231
308.15	0.9489	0.0235
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	0.0481
298.15	1.0000	0.0369
303.15	1.0000	0.0296
308.15	1.0000	0.0237

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.2500	293.85	0.0192
0.2500	313.05	0.0086
0.2500	333.05	0.0045
0.2500	353.05	0.0027
0.2500	382.15	0.0015
0.2500	393.35	0.0013
0.2500	409.75	0.0010
0.2500	427.35	0.0008
0.2500	446.45	0.0007
0.5000	294.05	0.0360
0.5000	313.05	0.0152
0.5000	333.05	0.0075
0.5000	353.05	0.0043
0.5000	386.75	0.0021
0.5000	395.35	0.0018
0.5000	411.85	0.0014
0.5000	429.95	0.0011
0.5000	447.45	0.0009
0.7500	294.15	0.0432
0.7500	313.05	0.0183
0.7500	333.05	0.0090
0.7500	353.05	0.0052
0.7500	387.45	0.0024
0.7500	396.55	0.0021
0.7500	411.45	0.0017
0.7500	429.35	0.0013
0.7500	448.55	0.0010

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Triethylene glycol (1) - Liquid	Viscosity, Pa*s - Liquid
302.85	1.0000	0.0271
307.75	1.0000	0.0197
312.65	1.0000	0.0159
317.45	1.0000	0.0130
322.25	1.0000	0.0103
327.05	1.0000	0.0080
332.15	1.0000	0.0053
341.45	1.0000	0.0016
302.85	0.9100	0.0204
307.75	0.9100	0.0154
312.65	0.9100	0.0123
317.45	0.9100	0.0102
322.25	0.9100	0.0081
327.05	0.9100	0.0063
332.15	0.9100	0.0042
341.45	0.9100	0.0013
302.85	0.8200	0.0149
307.75	0.8200	0.0112
312.65	0.8200	0.0090
317.45	0.8200	0.0075
322.25	0.8200	0.0060
327.05	0.8200	0.0047
332.15	0.8200	0.0032
341.45	0.8200	0.0010
302.85	0.7200	0.0098
307.75	0.7200	0.0075
312.65	0.7200	0.0062
317.45	0.7200	0.0051
322.25	0.7200	0.0041
327.05	0.7200	0.0033
332.15	0.7200	0.0023
341.45	0.7200	0.0007

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0250	0.0019
293.15	0.0489	0.0029
293.15	0.0754	0.0044
293.15	0.0993	0.0060
293.15	0.1500	0.0102
293.15	0.1993	0.0145
293.15	0.2526	0.0194
293.15	0.2998	0.0236
293.15	0.3539	0.0278
293.15	0.4009	0.0312
293.15	0.4492	0.0341
293.15	0.4992	0.0367
293.15	0.5484	0.0388
293.15	0.5996	0.0406
293.15	0.6506	0.0421
293.15	0.7010	0.0437
293.15	0.7567	0.0449
293.15	0.8035	0.0457
293.15	0.8406	0.0464
293.15	0.8981	0.0470
293.15	0.9489	0.0476
298.15	0.0250	0.0015
298.15	0.0489	0.0023
298.15	0.0754	0.0035
298.15	0.0993	0.0047
298.15	0.1500	0.0078
298.15	0.1993	0.0112
298.15	0.2526	0.0149
298.15	0.2998	0.0181
298.15	0.3539	0.0213
298.15	0.4009	0.0238
298.15	0.4492	0.0261
298.15	0.4992	0.0280
298.15	0.5484	0.0297
298.15	0.5996	0.0311
298.15	0.6506	0.0322
298.15	0.7010	0.0333
298.15	0.7567	0.0343
298.15	0.8035	0.0350
298.15	0.8406	0.0355
298.15	0.8981	0.0359
298.15	0.9489	0.0365
303.15	0.0250	0.0014
303.15	0.0489	0.0021
303.15	0.0754	0.0031
303.15	0.0993	0.0041
303.15	0.1500	0.0067
303.15	0.1993	0.0095
303.15	0.2526	0.0124
303.15	0.2998	0.0149
303.15	0.3539	0.0174
303.15	0.4009	0.0193
303.15	0.4492	0.0211
303.15	0.4992	0.0226
303.15	0.5484	0.0239
303.15	0.5996	0.0250
303.15	0.6506	0.0259
303.15	0.7010	0.0268
303.15	0.7567	0.0275
303.15	0.8035	0.0281
303.15	0.8406	0.0285
303.15	0.8981	0.0289
303.15	0.9489	0.0293
308.15	0.0250	0.0013
308.15	0.0489	0.0019
308.15	0.0754	0.0027
308.15	0.0993	0.0036
308.15	0.1500	0.0056
308.15	0.1993	0.0080
308.15	0.2526	0.0103
308.15	0.2998	0.0123
308.15	0.3539	0.0142
308.15	0.4009	0.0157
308.15	0.4492	0.0170
308.15	0.4992	0.0182
308.15	0.5484	0.0192
308.15	0.5996	0.0201
308.15	0.6506	0.0208
308.15	0.7010	0.0215
308.15	0.7567	0.0221
308.15	0.8035	0.0225
308.15	0.8406	0.0228
308.15	0.8981	0.0231
308.15	0.9489	0.0235
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	0.0481
298.15	1.0000	0.0369
303.15	1.0000	0.0296
308.15	1.0000	0.0237

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.2500	293.85	0.0192
0.2500	313.05	0.0086
0.2500	333.05	0.0045
0.2500	353.05	0.0027
0.2500	382.15	0.0015
0.2500	393.35	0.0013
0.2500	409.75	0.0010
0.2500	427.35	0.0008
0.2500	446.45	0.0007
0.5000	294.05	0.0360
0.5000	313.05	0.0152
0.5000	333.05	0.0075
0.5000	353.05	0.0043
0.5000	386.75	0.0021
0.5000	395.35	0.0018
0.5000	411.85	0.0014
0.5000	429.95	0.0011
0.5000	447.45	0.0009
0.7500	294.15	0.0432
0.7500	313.05	0.0183
0.7500	333.05	0.0090
0.7500	353.05	0.0052
0.7500	387.45	0.0024
0.7500	396.55	0.0021
0.7500	411.45	0.0017
0.7500	429.35	0.0013
0.7500	448.55	0.0010

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Triethylene glycol (1) - Liquid	Viscosity, Pa*s - Liquid
302.85	1.0000	0.0271
307.75	1.0000	0.0197
312.65	1.0000	0.0159
317.45	1.0000	0.0130
322.25	1.0000	0.0103
327.05	1.0000	0.0080
332.15	1.0000	0.0053
341.45	1.0000	0.0016
302.85	0.9100	0.0204
307.75	0.9100	0.0154
312.65	0.9100	0.0123
317.45	0.9100	0.0102
322.25	0.9100	0.0081
327.05	0.9100	0.0063
332.15	0.9100	0.0042
341.45	0.9100	0.0013
302.85	0.8200	0.0149
307.75	0.8200	0.0112
312.65	0.8200	0.0090
317.45	0.8200	0.0075
322.25	0.8200	0.0060
327.05	0.8200	0.0047
332.15	0.8200	0.0032
341.45	0.8200	0.0010
302.85	0.7200	0.0098
307.75	0.7200	0.0075
312.65	0.7200	0.0062
317.45	0.7200	0.0051
322.25	0.7200	0.0041
327.05	0.7200	0.0033
332.15	0.7200	0.0023
341.45	0.7200	0.0007

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
0.1291	-0.4400
0.2167	-0.7870
0.3145	-1.079
0.4016	-1.34
0.5006	-1.606
0.6006	-1.803
0.6999	-1.876
0.7985	-1.767
0.9013	-1.307

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
0.1291	-0.4400
0.2167	-0.7870
0.3145	-1.079
0.4016	-1.34
0.5006	-1.606
0.6006	-1.803
0.6999	-1.876
0.7985	-1.767
0.9013	-1.307

Joule-Thomson coefficient, K/kPa [ref]

Operational condition: Pressure, kPa = 7000 (Liquid)

Fixed		Measured
Mass fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Joule-Thomson coefficient, K/kPa - Liquid
0.0000	293.40	-0.0002
0.9900	293.80	-0.0003
1.0000	293.10	-0.0004

Joule-Thomson coefficient, K/kPa [ref]

Operational condition: Pressure, kPa = 7000 (Liquid)

Fixed		Measured
Mass fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Joule-Thomson coefficient, K/kPa - Liquid
0.0000	293.40	-0.0002
0.9900	293.80	-0.0003
1.0000	293.10	-0.0004

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
0.1000	1.442
0.2100	1.4305
0.3000	1.4199
0.4100	1.4064
0.5000	1.3941
0.6000	1.3818
0.7000	1.3684
0.8000	1.3562
0.9000	1.3438
1.0000	1.3318

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
0.1000	1.442
0.2100	1.4305
0.3000	1.4199
0.4100	1.4064
0.5000	1.3941
0.6000	1.3818
0.7000	1.3684
0.8000	1.3562
0.9000	1.3438
1.0000	1.3318

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0000	999.965
278.15	0.0107	1013.307
278.15	0.0205	1024.392
278.15	0.0397	1043.405
278.15	0.0498	1051.97
278.15	0.0700	1066.643
278.15	0.0942	1080.565
278.15	0.1481	1100.994
278.15	0.2006	1112.251
278.15	0.2502	1118.669
278.15	0.2988	1122.733
278.15	0.3492	1125.607
278.15	0.3925	1127.4
278.15	0.4502	1129.181
278.15	0.4877	1130.078
278.15	0.5004	1130.346
278.15	0.5739	1131.636
278.15	0.5800	1131.726
278.15	0.6510	1132.63
278.15	0.6465	1132.58
278.15	0.7008	1133.138
278.15	0.7471	1133.542
278.15	0.7677	1133.705
278.15	0.8200	1134.079
278.15	0.8792	1134.452
278.15	0.8623	1134.35
278.15	0.8975	1134.559
278.15	0.9203	1134.69
278.15	0.9514	1134.864
278.15	0.9692	1134.964
278.15	1.0000	1135.136
283.15	0.0000	999.698
283.15	0.0107	1012.653
283.15	0.0205	1023.405
283.15	0.0397	1041.831
283.15	0.0498	1050.129
283.15	0.0700	1064.346
283.15	0.0942	1077.848
283.15	0.1481	1097.71
283.15	0.2006	1108.705
283.15	0.2502	1115.004
283.15	0.2988	1119.011
283.15	0.3492	1121.856
283.15	0.3925	1123.636
283.15	0.4502	1125.409
283.15	0.4877	1126.302
283.15	0.5004	1126.569
283.15	0.5739	1127.851
283.15	0.5800	1127.941
283.15	0.6510	1128.835
283.15	0.6465	1128.786
283.15	0.7008	1129.336
283.15	0.7471	1129.733
283.15	0.7677	1129.892
283.15	0.8200	1130.259
283.15	0.8792	1130.624
283.15	0.8623	1130.524
283.15	0.8975	1130.729
283.15	0.9203	1130.857
283.15	0.9514	1131.027
283.15	0.9692	1131.124
283.15	1.0000	1131.291
288.15	0.0000	999.099
288.15	0.0107	1011.719
288.15	0.0205	1022.175
288.15	0.0397	1040.073
288.15	0.0498	1048.128
288.15	0.0700	1061.931
288.15	0.0942	1075.048
288.15	0.1481	1094.389
288.15	0.2006	1105.141
288.15	0.2502	1111.325
288.15	0.2988	1115.274
288.15	0.3492	1118.089
288.15	0.3925	1119.856
288.15	0.4502	1121.618
288.15	0.4877	1122.508
288.15	0.5004	1122.773
288.15	0.5739	1124.046
288.15	0.5800	1124.135
288.15	0.6510	1125.018
288.15	0.6465	1124.97
288.15	0.7008	1125.511
288.15	0.7471	1125.901
288.15	0.7677	1126.057
288.15	0.8200	1126.418
288.15	0.8792	1126.777
288.15	0.8623	1126.679
288.15	0.8975	1126.881
288.15	0.9203	1127.007
288.15	0.9514	1127.174
288.15	0.9692	1127.268
288.15	1.0000	1127.429
293.15	0.0000	998.204
293.15	0.0107	1010.533
293.15	0.0205	1020.726
293.15	0.0397	1038.141
293.15	0.0498	1045.972
293.15	0.0700	1059.386
293.15	0.0942	1072.144
293.15	0.1481	1090.998
293.15	0.2006	1101.526
293.15	0.2502	1107.607
293.15	0.2988	1111.507
293.15	0.3492	1114.298
293.15	0.3925	1116.057
293.15	0.4502	1117.814
293.15	0.4877	1118.701
293.15	0.5004	1118.966
293.15	0.5739	1120.23
293.15	0.5800	1120.318
293.15	0.6510	1121.19
293.15	0.6465	1121.143
293.15	0.7008	1121.675
293.15	0.7471	1122.058
293.15	0.7677	1122.213
293.15	0.8200	1122.569
293.15	0.8792	1122.927
293.15	0.8623	1122.829
293.15	0.8975	1123.03
293.15	0.9203	1123.154
293.15	0.9514	1123.318
293.15	0.9692	1123.409
293.15	1.0000	1123.562
298.15	0.0000	997.043
298.15	0.0107	1009.152
298.15	0.0205	1019.125
298.15	0.0397	1036.101
298.15	0.0498	1043.715
298.15	0.0700	1056.746
298.15	0.0942	1069.14
298.15	0.1481	1087.524
298.15	0.2006	1097.869
298.15	0.2502	1103.885
298.15	0.2988	1107.755
298.15	0.3492	1110.521
298.15	0.3925	1112.259
298.15	0.4502	1113.992
298.15	0.4877	1114.868
298.15	0.5004	1115.129
298.15	0.5739	1116.385
298.15	0.5800	1116.473
298.15	0.6510	1117.347
298.15	0.6465	1117.299
298.15	0.7008	1117.833
298.15	0.7471	1118.216
298.15	0.7677	1118.369
298.15	0.8200	1118.718
298.15	0.8792	1119.063
298.15	0.8623	1118.969
298.15	0.8975	1119.162
298.15	0.9203	1119.282
298.15	0.9514	1119.442
298.15	0.9692	1119.533
298.15	1.0000	1119.69
303.15	0.0000	995.643
303.15	0.0107	1007.527
303.15	0.0205	1017.291
303.15	0.0397	1033.872
303.15	0.0498	1041.298
303.15	0.0700	1053.998
303.15	0.0942	1066.077
303.15	0.1481	1084.031
303.15	0.2006	1094.183
303.15	0.2502	1100.117
303.15	0.2988	1103.95
303.15	0.3492	1106.698
303.15	0.3925	1108.428
303.15	0.4502	1110.156
303.15	0.4877	1111.029
303.15	0.5004	1111.29
303.15	0.5739	1112.541
303.15	0.5800	1112.629
303.15	0.6510	1113.498
303.15	0.6465	1113.45
303.15	0.7008	1113.981
303.15	0.7471	1114.361
303.15	0.7677	1114.512
303.15	0.8200	1114.858
303.15	0.8792	1115.198
303.15	0.8623	1115.105
303.15	0.8975	1115.295
303.15	0.9203	1115.413
303.15	0.9514	1115.569
303.15	0.9692	1115.657
303.15	1.0000	1115.809
308.15	0.0000	994.026
308.15	0.0107	1005.7
308.15	0.0205	1015.27
308.15	0.0397	1031.49
308.15	0.0498	1038.745
308.15	0.0700	1051.146
308.15	0.0942	1062.94
308.15	0.1481	1080.499
308.15	0.2006	1090.467
308.15	0.2502	1096.32
308.15	0.2988	1100.116
308.15	0.3492	1102.849
308.15	0.3925	1104.574
308.15	0.4502	1106.299
308.15	0.4877	1107.171
308.15	0.5004	1107.432
308.15	0.5739	1108.682
308.15	0.5800	1108.769
308.15	0.6510	1109.635
308.15	0.6465	1109.588
308.15	0.7008	1110.116
308.15	0.7471	1110.493
308.15	0.7677	1110.644
308.15	0.8200	1110.987
308.15	0.8792	1111.324
308.15	0.8623	1111.233
308.15	0.8975	1111.421
308.15	0.9203	1111.537
308.15	0.9514	1111.69
308.15	0.9692	1111.776
308.15	1.0000	1111.924
313.15	0.0000	992.208
313.15	0.0107	1003.694
313.15	0.0205	1013.088
313.15	0.0397	1028.974
313.15	0.0498	1036.069
313.15	0.0700	1048.188
313.15	0.0942	1059.716
313.15	0.1481	1076.91
313.15	0.2006	1086.714
313.15	0.2502	1092.497
313.15	0.2988	1096.262
313.15	0.3492	1098.979
313.15	0.3925	1100.698
313.15	0.4502	1102.421
313.15	0.4877	1103.293
313.15	0.5004	1103.553
313.15	0.5739	1104.804
313.15	0.5800	1104.891
313.15	0.6510	1105.757
313.15	0.6465	1105.71
313.15	0.7008	1106.237
313.15	0.7471	1106.613
313.15	0.7677	1106.763
313.15	0.8200	1107.105
313.15	0.8792	1107.44
313.15	0.8623	1107.349
313.15	0.8975	1107.535
313.15	0.9203	1107.65
313.15	0.9514	1107.801
313.15	0.9692	1107.886
313.15	1.0000	1108.031
318.15	0.0000	990.201
318.15	0.0107	1001.514
318.15	0.0205	1010.746
318.15	0.0397	1026.324
318.15	0.0498	1033.271
318.15	0.0700	1045.13
318.15	0.0942	1056.411
318.15	0.1481	1073.267
318.15	0.2006	1082.92
318.15	0.2502	1088.64
318.15	0.2988	1092.378
318.15	0.3492	1095.085
318.15	0.3925	1096.802
318.15	0.4502	1098.526
318.15	0.4877	1099.4
318.15	0.5004	1099.661
318.15	0.5739	1100.916
318.15	0.5800	1101.003
318.15	0.6510	1101.871
318.15	0.6465	1101.824
318.15	0.7008	1102.351
318.15	0.7471	1102.727
318.15	0.7677	1102.876
318.15	0.8200	1103.216
318.15	0.8792	1103.548
318.15	0.8623	1103.458
318.15	0.8975	1103.642
318.15	0.9203	1103.756
318.15	0.9514	1103.905
318.15	0.9692	1103.989
318.15	1.0000	1104.132
323.15	0.0000	988.027
323.15	0.0107	999.177
323.15	0.0205	1008.259
323.15	0.0397	1023.558
323.15	0.0498	1030.371
323.15	0.0700	1041.993
323.15	0.0942	1053.042
323.15	0.1481	1069.567
323.15	0.2006	1079.068
323.15	0.2502	1084.728
323.15	0.2988	1088.448
323.15	0.3492	1091.154
323.15	0.3925	1092.875
323.15	0.4502	1094.607
323.15	0.4877	1095.484
323.15	0.5004	1095.747
323.15	0.5739	1097.006
323.15	0.5800	1097.094
323.15	0.6510	1097.964
323.15	0.6465	1097.916
323.15	0.7008	1098.445
323.15	0.7471	1098.821
323.15	0.7677	1098.971
323.15	0.8200	1099.312
323.15	0.8792	1099.645
323.15	0.8623	1099.555
323.15	0.8975	1099.74
323.15	0.9203	1099.853
323.15	0.9514	1100.001
323.15	0.9692	1100.084
323.15	1.0000	1100.224
328.15	0.0000	985.682
328.15	0.0107	996.693
328.15	0.0205	1005.638
328.15	0.0397	1020.667
328.15	0.0498	1027.35
328.15	0.0700	1038.742
328.15	0.0942	1049.576
328.15	0.1481	1065.819
328.15	0.2006	1075.203
328.15	0.2502	1080.818
328.15	0.2988	1084.517
328.15	0.3492	1087.214
328.15	0.3925	1088.933
328.15	0.4502	1090.665
328.15	0.4877	1091.545
328.15	0.5004	1091.809
328.15	0.5739	1093.076
328.15	0.5800	1093.165
328.15	0.6510	1094.043
328.15	0.6465	1093.995
328.15	0.7008	1094.529
328.15	0.7471	1094.908
328.15	0.7677	1095.059
328.15	0.8200	1095.401
328.15	0.8792	1095.733
328.15	0.8623	1095.643
328.15	0.8975	1095.826
328.15	0.9203	1095.938
328.15	0.9514	1096.085
328.15	0.9692	1096.166
328.15	1.0000	1096.304
333.15	0.0000	983.186
333.15	0.0107	994.065
333.15	0.0205	1002.886
333.15	0.0397	1017.675
333.15	0.0498	1024.24
333.15	0.0700	1035.424
333.15	0.0942	1046.055
333.15	0.1481	1062.017
333.15	0.2006	1071.276
333.15	0.2502	1076.844
333.15	0.2988	1080.531
333.15	0.3492	1083.23
333.15	0.3925	1084.955
333.15	0.4502	1086.697
333.15	0.4877	1087.583
333.15	0.5004	1087.849
333.15	0.5739	1089.126
333.15	0.5800	1089.215
333.15	0.6510	1090.101
333.15	0.6465	1090.053
333.15	0.7008	1090.592
333.15	0.7471	1090.974
333.15	0.7677	1091.127
333.15	0.8200	1091.471
333.15	0.8792	1091.805
333.15	0.8623	1091.715
333.15	0.8975	1091.9
333.15	0.9203	1092.012
333.15	0.9514	1092.159
333.15	0.9692	1092.241
333.15	1.0000	1092.378

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0101	1009.83
293.15	0.0196	1019.709
293.15	0.0290	1028.875
293.15	0.0381	1036.741
293.15	0.0496	1045.761
293.15	0.0601	1053.181
293.15	0.0689	1058.687
293.15	0.0801	1065.0
293.15	0.0905	1070.231
293.15	0.0996	1074.379
293.15	0.1479	1090.644
293.15	0.2004	1101.267
293.15	0.2462	1107.121
293.15	0.3004	1111.57
293.15	0.3474	1114.222
293.15	0.3948	1116.154
293.15	0.4467	1117.712
293.15	0.5021	1118.967
293.15	0.5480	1119.771
293.15	0.5923	1120.433
293.15	0.6442	1121.04
293.15	0.7095	1121.664
293.15	0.7531	1122.027
293.15	0.7859	1122.278
293.15	0.8387	1122.621
293.15	0.9031	1123.012
293.15	0.9181	1123.079
293.15	0.9344	1123.16
293.15	0.9569	1123.277
293.15	0.9782	1123.366
298.15	0.0101	1008.379
298.15	0.0196	1017.879
298.15	0.0290	1027.039
298.15	0.0381	1034.701
298.15	0.0496	1043.48
298.15	0.0601	1050.699
298.15	0.0689	1056.054
298.15	0.0801	1062.197
298.15	0.0905	1067.29
298.15	0.0996	1071.333
298.15	0.1479	1087.214
298.15	0.2004	1097.629
298.15	0.2462	1103.393
298.15	0.3004	1107.789
298.15	0.3474	1110.414
298.15	0.3948	1112.332
298.15	0.4467	1113.88
298.15	0.5021	1115.129
298.15	0.5480	1115.929
298.15	0.5923	1116.587
298.15	0.6442	1117.188
298.15	0.7095	1117.805
298.15	0.7531	1118.169
298.15	0.7859	1118.416
298.15	0.8387	1118.746
298.15	0.9031	1119.131
298.15	0.9181	1119.196
298.15	0.9344	1119.278
298.15	0.9569	1119.392
298.15	0.9782	1119.477
303.15	0.0101	1006.695
303.15	0.0196	1016.055
303.15	0.0290	1025.028
303.15	0.0381	1032.503
303.15	0.0496	1041.066
303.15	0.0601	1048.097
303.15	0.0689	1053.316
303.15	0.0801	1059.303
303.15	0.0905	1064.27
303.15	0.0996	1068.21
303.15	0.1479	1083.731
303.15	0.2004	1093.951
303.15	0.2462	1099.632
303.15	0.3004	1103.987
303.15	0.3474	1106.587
303.15	0.3948	1108.496
303.15	0.4467	1110.038
303.15	0.5021	1111.282
303.15	0.5480	1112.08
303.15	0.5923	1112.734
303.15	0.6442	1113.331
303.15	0.7095	1113.945
303.15	0.7531	1114.304
303.15	0.7859	1114.547
303.15	0.8387	1114.874
303.15	0.9031	1115.252
303.15	0.9181	1115.312
303.15	0.9344	1115.396
303.15	0.9569	1115.503
303.15	0.9782	1115.592
308.15	0.0101	1005.032
308.15	0.0196	1014.271
308.15	0.0290	1022.856
308.15	0.0381	1030.162
308.15	0.0496	1038.523
308.15	0.0601	1045.381
308.15	0.0689	1050.481
308.15	0.0801	1056.319
308.15	0.0905	1061.171
308.15	0.0996	1065.013
308.15	0.1479	1080.199
308.15	0.2004	1090.242
308.15	0.2462	1095.849
308.15	0.3004	1100.159
308.15	0.3474	1102.741
308.15	0.3948	1104.642
308.15	0.4467	1106.18
308.15	0.5021	1107.423
308.15	0.5480	1108.218
308.15	0.5923	1108.871
308.15	0.6442	1109.464
308.15	0.7095	1110.082
308.15	0.7531	1110.432
308.15	0.7859	1110.677
308.15	0.8387	1110.998
308.15	0.9031	1111.373
308.15	0.9181	1111.423
308.15	0.9344	1111.515
308.15	0.9569	1111.619
308.15	0.9782	1111.707
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	1123.477
298.15	1.0000	1119.586
303.15	1.0000	1115.703
308.15	1.0000	1111.814
293.15	0.0250	1024.911
293.15	0.0489	1044.887
293.15	0.0754	1062.235
293.15	0.0993	1074.348
293.15	0.1500	1091.94
293.15	0.1993	1101.822
293.15	0.2526	1107.939
293.15	0.2998	1111.261
293.15	0.3539	1113.94
293.15	0.4009	1115.826
293.15	0.4492	1117.526
293.15	0.4992	1119.037
293.15	0.5484	1120.205
293.15	0.5996	1121.027
293.15	0.6506	1121.459
293.15	0.7010	1121.616
293.15	0.7567	1121.705
293.15	0.8035	1121.913
293.15	0.8406	1122.247
293.15	0.8981	1123.022
293.15	0.9489	1123.572
298.15	0.0250	1023.095
298.15	0.0489	1042.583
298.15	0.0754	1059.509
298.15	0.0993	1071.331
298.15	0.1500	1088.51
298.15	0.1993	1098.179
298.15	0.2526	1104.187
298.15	0.2998	1107.47
298.15	0.3539	1110.13
298.15	0.4009	1112.009
298.15	0.4492	1113.702
298.15	0.4992	1115.204
298.15	0.5484	1116.361
298.15	0.5996	1117.175
298.15	0.6506	1117.601
298.15	0.7010	1117.756
298.15	0.7567	1117.845
298.15	0.8035	1118.05
298.15	0.8406	1118.38
298.15	0.8981	1119.145
298.15	0.9489	1119.685
303.15	0.0250	1021.124
303.15	0.0489	1040.158
303.15	0.0754	1056.69
303.15	0.0993	1068.238
303.15	0.1500	1085.03
303.15	0.1993	1094.498
303.15	0.2526	1100.405
303.15	0.2998	1103.652
303.15	0.3539	1106.301
303.15	0.4009	1108.177
303.15	0.4492	1109.867
303.15	0.4992	1111.363
303.15	0.5484	1112.514
303.15	0.5996	1113.319
303.15	0.6506	1113.74
303.15	0.7010	1113.891
303.15	0.7567	1113.977
303.15	0.8035	1114.181
303.15	0.8406	1114.508
303.15	0.8981	1115.265
303.15	0.9489	1115.798
308.15	0.0250	1019.054
308.15	0.0489	1037.636
308.15	0.0754	1053.782
308.15	0.0993	1065.065
308.15	0.1500	1081.49
308.15	0.1993	1090.776
308.15	0.2526	1096.597
308.15	0.2998	1099.817
308.15	0.3539	1102.458
308.15	0.4009	1104.332
308.15	0.4492	1106.018
308.15	0.4992	1107.509
308.15	0.5484	1108.652
308.15	0.5996	1109.451
308.15	0.6506	1109.869
308.15	0.7010	1110.021
308.15	0.7567	1110.109
308.15	0.8035	1110.313
308.15	0.8406	1110.638
308.15	0.8981	1111.387
308.15	0.9489	1111.911

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0965	1000.31
293.15	0.2002	1002.46
293.15	0.2920	1004.29
293.15	0.3986	1006.36
293.15	0.4988	1008.22
303.15	0.0965	997.73
303.15	0.2002	999.86
303.15	0.2920	1001.67
303.15	0.3986	1003.69
303.15	0.4988	1005.54
293.15	0.0000	998.21
303.15	0.0000	995.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0544	1001.214
278.15	0.1018	1002.295
278.15	0.2012	1004.531
278.15	0.3025	1006.774
278.15	0.4009	1008.917
283.15	0.0544	1000.922
283.15	0.1018	1001.977
283.15	0.2012	1004.153
283.15	0.3025	1006.338
283.15	0.4009	1008.423
288.15	0.0544	1000.298
288.15	0.1018	1001.329
288.15	0.2012	1003.456
288.15	0.3025	1005.59
288.15	0.4009	1007.625
293.15	0.0544	999.38
293.15	0.1018	1000.39
293.15	0.2012	1002.475
293.15	0.3025	1004.565
293.15	0.4009	1006.553
298.15	0.0544	998.2
298.15	0.1018	999.192
298.15	0.2012	1001.241
298.15	0.3025	1003.288
298.15	0.4009	1005.239
303.15	0.0544	996.785
303.15	0.1018	997.76
303.15	0.2012	999.776
303.15	0.3025	1001.787
303.15	0.4009	1003.7
308.15	0.0544	995.154
308.15	0.1018	996.109
308.15	0.2012	998.097
308.15	0.3025	1000.076
308.15	0.4009	1001.956
313.15	0.0544	993.322
313.15	0.1018	994.268
313.15	0.2012	996.223
313.15	0.3025	998.171
313.15	0.4009	1000.021
318.15	0.0544	991.307
318.15	0.1018	992.24
318.15	0.2012	994.166
318.15	0.3025	996.086
318.15	0.4009	997.909
323.15	0.0544	989.117
323.15	0.1018	990.037
323.15	0.2012	991.939
323.15	0.3025	993.832
323.15	0.4009	995.628
328.15	0.0544	986.763
328.15	0.1018	987.673
328.15	0.2012	989.548
328.15	0.3025	991.417
328.15	0.4009	993.188
333.15	0.0544	984.253
333.15	0.1018	985.152
333.15	0.2012	987.006
333.15	0.3025	988.85
333.15	0.4009	990.597
338.15	0.0544	981.597
338.15	0.1018	982.485
338.15	0.2012	984.316
338.15	0.3025	986.139
338.15	0.4009	987.864
343.15	0.0544	978.8
343.15	0.1018	979.677
343.15	0.2012	981.488
343.15	0.3025	983.288
343.15	0.4009	984.994

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0965	1001.366
288.15	0.2002	1003.551
288.15	0.2920	1005.416
288.15	0.3986	1007.496
288.15	0.4988	1009.367
288.15	0.5999	1011.202
288.15	0.6947	1012.819
288.15	0.7929	1014.471
298.15	0.0965	999.126
298.15	0.2002	1001.272
298.15	0.2920	1003.106
298.15	0.3986	1005.14
298.15	0.4988	1006.991
298.15	0.5999	1008.767
298.15	0.6947	1010.377
298.15	0.7929	1011.992
308.15	0.0965	996.095
308.15	0.2002	998.216
308.15	0.2920	1000.013
308.15	0.3986	1002.025
308.15	0.4988	1003.851
308.15	0.5999	1005.625
308.15	0.6947	1007.215
308.15	0.7929	1008.811
318.15	0.0965	992.405
318.15	0.2002	994.52
318.15	0.2920	996.322
318.15	0.3986	998.332
318.15	0.4988	1000.147
318.15	0.5999	1001.923
318.15	0.6947	1003.518
318.15	0.7929	1005.119

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Molality, mol/kg of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0965	293.15	1000.308
0.2002	293.15	1002.462
0.2920	293.15	1004.291
0.3986	293.15	1006.356
0.4988	293.15	1008.223
0.0965	298.15	999.126
0.2002	298.15	1001.272
0.2920	298.15	1003.106
0.3986	298.15	1005.14
0.4988	298.15	1006.991
0.0965	303.15	997.728
0.2002	303.15	999.858
0.2920	303.15	1001.668
0.3986	303.15	1003.693
0.4988	303.15	1005.54
0.0965	308.15	996.095
0.2002	308.15	998.216
0.2920	308.15	1000.013
0.3986	308.15	1002.025
0.4988	308.15	1003.851

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.2500	293.85	1108.0
0.2500	313.05	1093.0
0.2500	333.05	1078.0
0.2500	353.05	1061.0
0.2500	379.65	1039.0
0.2500	389.35	1030.0
0.2500	405.75	1016.0
0.2500	423.35	999.2
0.2500	442.45	980.0
0.5000	294.05	1120.0
0.5000	313.05	1105.0
0.5000	333.05	1089.0
0.5000	353.05	1073.0
0.5000	384.25	1046.0
0.5000	391.35	1041.0
0.5000	407.85	1028.0
0.5000	425.95	1011.0
0.5000	443.45	995.0
0.7500	294.15	1122.0
0.7500	313.05	1108.0
0.7500	333.05	1092.0
0.7500	353.05	1076.0
0.7500	384.95	1049.0
0.7500	392.55	1044.0
0.7500	407.45	1032.0
0.7500	425.35	1016.0
0.7500	444.55	999.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
302.85	1.0000	1116.6
307.75	1.0000	1111.9
312.65	1.0000	1108.4
317.45	1.0000	1104.7
322.25	1.0000	1101.0
327.05	1.0000	1097.9
332.15	1.0000	1093.5
341.45	1.0000	1086.1
302.85	0.9100	1111.7
307.75	0.9100	1108.3
312.65	0.9100	1103.9
317.45	0.9100	1100.5
322.25	0.9100	1097.0
327.05	0.9100	1093.9
332.15	0.9100	1089.6
341.45	0.9100	1083.2
302.85	0.8200	1106.6
307.75	0.8200	1102.6
312.65	0.8200	1098.6
317.45	0.8200	1094.5
322.25	0.8200	1091.0
327.05	0.8200	1087.6
332.15	0.8200	1083.8
341.45	0.8200	1075.9
302.85	0.7200	1096.9
307.75	0.7200	1094.2
312.65	0.7200	1090.2
317.45	0.7200	1086.3
322.25	0.7200	1082.8
327.05	0.7200	1079.3
332.15	0.7200	1075.3
341.45	0.7200	1067.4

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0000	999.965
278.15	0.0107	1013.307
278.15	0.0205	1024.392
278.15	0.0397	1043.405
278.15	0.0498	1051.97
278.15	0.0700	1066.643
278.15	0.0942	1080.565
278.15	0.1481	1100.994
278.15	0.2006	1112.251
278.15	0.2502	1118.669
278.15	0.2988	1122.733
278.15	0.3492	1125.607
278.15	0.3925	1127.4
278.15	0.4502	1129.181
278.15	0.4877	1130.078
278.15	0.5004	1130.346
278.15	0.5739	1131.636
278.15	0.5800	1131.726
278.15	0.6510	1132.63
278.15	0.6465	1132.58
278.15	0.7008	1133.138
278.15	0.7471	1133.542
278.15	0.7677	1133.705
278.15	0.8200	1134.079
278.15	0.8792	1134.452
278.15	0.8623	1134.35
278.15	0.8975	1134.559
278.15	0.9203	1134.69
278.15	0.9514	1134.864
278.15	0.9692	1134.964
278.15	1.0000	1135.136
283.15	0.0000	999.698
283.15	0.0107	1012.653
283.15	0.0205	1023.405
283.15	0.0397	1041.831
283.15	0.0498	1050.129
283.15	0.0700	1064.346
283.15	0.0942	1077.848
283.15	0.1481	1097.71
283.15	0.2006	1108.705
283.15	0.2502	1115.004
283.15	0.2988	1119.011
283.15	0.3492	1121.856
283.15	0.3925	1123.636
283.15	0.4502	1125.409
283.15	0.4877	1126.302
283.15	0.5004	1126.569
283.15	0.5739	1127.851
283.15	0.5800	1127.941
283.15	0.6510	1128.835
283.15	0.6465	1128.786
283.15	0.7008	1129.336
283.15	0.7471	1129.733
283.15	0.7677	1129.892
283.15	0.8200	1130.259
283.15	0.8792	1130.624
283.15	0.8623	1130.524
283.15	0.8975	1130.729
283.15	0.9203	1130.857
283.15	0.9514	1131.027
283.15	0.9692	1131.124
283.15	1.0000	1131.291
288.15	0.0000	999.099
288.15	0.0107	1011.719
288.15	0.0205	1022.175
288.15	0.0397	1040.073
288.15	0.0498	1048.128
288.15	0.0700	1061.931
288.15	0.0942	1075.048
288.15	0.1481	1094.389
288.15	0.2006	1105.141
288.15	0.2502	1111.325
288.15	0.2988	1115.274
288.15	0.3492	1118.089
288.15	0.3925	1119.856
288.15	0.4502	1121.618
288.15	0.4877	1122.508
288.15	0.5004	1122.773
288.15	0.5739	1124.046
288.15	0.5800	1124.135
288.15	0.6510	1125.018
288.15	0.6465	1124.97
288.15	0.7008	1125.511
288.15	0.7471	1125.901
288.15	0.7677	1126.057
288.15	0.8200	1126.418
288.15	0.8792	1126.777
288.15	0.8623	1126.679
288.15	0.8975	1126.881
288.15	0.9203	1127.007
288.15	0.9514	1127.174
288.15	0.9692	1127.268
288.15	1.0000	1127.429
293.15	0.0000	998.204
293.15	0.0107	1010.533
293.15	0.0205	1020.726
293.15	0.0397	1038.141
293.15	0.0498	1045.972
293.15	0.0700	1059.386
293.15	0.0942	1072.144
293.15	0.1481	1090.998
293.15	0.2006	1101.526
293.15	0.2502	1107.607
293.15	0.2988	1111.507
293.15	0.3492	1114.298
293.15	0.3925	1116.057
293.15	0.4502	1117.814
293.15	0.4877	1118.701
293.15	0.5004	1118.966
293.15	0.5739	1120.23
293.15	0.5800	1120.318
293.15	0.6510	1121.19
293.15	0.6465	1121.143
293.15	0.7008	1121.675
293.15	0.7471	1122.058
293.15	0.7677	1122.213
293.15	0.8200	1122.569
293.15	0.8792	1122.927
293.15	0.8623	1122.829
293.15	0.8975	1123.03
293.15	0.9203	1123.154
293.15	0.9514	1123.318
293.15	0.9692	1123.409
293.15	1.0000	1123.562
298.15	0.0000	997.043
298.15	0.0107	1009.152
298.15	0.0205	1019.125
298.15	0.0397	1036.101
298.15	0.0498	1043.715
298.15	0.0700	1056.746
298.15	0.0942	1069.14
298.15	0.1481	1087.524
298.15	0.2006	1097.869
298.15	0.2502	1103.885
298.15	0.2988	1107.755
298.15	0.3492	1110.521
298.15	0.3925	1112.259
298.15	0.4502	1113.992
298.15	0.4877	1114.868
298.15	0.5004	1115.129
298.15	0.5739	1116.385
298.15	0.5800	1116.473
298.15	0.6510	1117.347
298.15	0.6465	1117.299
298.15	0.7008	1117.833
298.15	0.7471	1118.216
298.15	0.7677	1118.369
298.15	0.8200	1118.718
298.15	0.8792	1119.063
298.15	0.8623	1118.969
298.15	0.8975	1119.162
298.15	0.9203	1119.282
298.15	0.9514	1119.442
298.15	0.9692	1119.533
298.15	1.0000	1119.69
303.15	0.0000	995.643
303.15	0.0107	1007.527
303.15	0.0205	1017.291
303.15	0.0397	1033.872
303.15	0.0498	1041.298
303.15	0.0700	1053.998
303.15	0.0942	1066.077
303.15	0.1481	1084.031
303.15	0.2006	1094.183
303.15	0.2502	1100.117
303.15	0.2988	1103.95
303.15	0.3492	1106.698
303.15	0.3925	1108.428
303.15	0.4502	1110.156
303.15	0.4877	1111.029
303.15	0.5004	1111.29
303.15	0.5739	1112.541
303.15	0.5800	1112.629
303.15	0.6510	1113.498
303.15	0.6465	1113.45
303.15	0.7008	1113.981
303.15	0.7471	1114.361
303.15	0.7677	1114.512
303.15	0.8200	1114.858
303.15	0.8792	1115.198
303.15	0.8623	1115.105
303.15	0.8975	1115.295
303.15	0.9203	1115.413
303.15	0.9514	1115.569
303.15	0.9692	1115.657
303.15	1.0000	1115.809
308.15	0.0000	994.026
308.15	0.0107	1005.7
308.15	0.0205	1015.27
308.15	0.0397	1031.49
308.15	0.0498	1038.745
308.15	0.0700	1051.146
308.15	0.0942	1062.94
308.15	0.1481	1080.499
308.15	0.2006	1090.467
308.15	0.2502	1096.32
308.15	0.2988	1100.116
308.15	0.3492	1102.849
308.15	0.3925	1104.574
308.15	0.4502	1106.299
308.15	0.4877	1107.171
308.15	0.5004	1107.432
308.15	0.5739	1108.682
308.15	0.5800	1108.769
308.15	0.6510	1109.635
308.15	0.6465	1109.588
308.15	0.7008	1110.116
308.15	0.7471	1110.493
308.15	0.7677	1110.644
308.15	0.8200	1110.987
308.15	0.8792	1111.324
308.15	0.8623	1111.233
308.15	0.8975	1111.421
308.15	0.9203	1111.537
308.15	0.9514	1111.69
308.15	0.9692	1111.776
308.15	1.0000	1111.924
313.15	0.0000	992.208
313.15	0.0107	1003.694
313.15	0.0205	1013.088
313.15	0.0397	1028.974
313.15	0.0498	1036.069
313.15	0.0700	1048.188
313.15	0.0942	1059.716
313.15	0.1481	1076.91
313.15	0.2006	1086.714
313.15	0.2502	1092.497
313.15	0.2988	1096.262
313.15	0.3492	1098.979
313.15	0.3925	1100.698
313.15	0.4502	1102.421
313.15	0.4877	1103.293
313.15	0.5004	1103.553
313.15	0.5739	1104.804
313.15	0.5800	1104.891
313.15	0.6510	1105.757
313.15	0.6465	1105.71
313.15	0.7008	1106.237
313.15	0.7471	1106.613
313.15	0.7677	1106.763
313.15	0.8200	1107.105
313.15	0.8792	1107.44
313.15	0.8623	1107.349
313.15	0.8975	1107.535
313.15	0.9203	1107.65
313.15	0.9514	1107.801
313.15	0.9692	1107.886
313.15	1.0000	1108.031
318.15	0.0000	990.201
318.15	0.0107	1001.514
318.15	0.0205	1010.746
318.15	0.0397	1026.324
318.15	0.0498	1033.271
318.15	0.0700	1045.13
318.15	0.0942	1056.411
318.15	0.1481	1073.267
318.15	0.2006	1082.92
318.15	0.2502	1088.64
318.15	0.2988	1092.378
318.15	0.3492	1095.085
318.15	0.3925	1096.802
318.15	0.4502	1098.526
318.15	0.4877	1099.4
318.15	0.5004	1099.661
318.15	0.5739	1100.916
318.15	0.5800	1101.003
318.15	0.6510	1101.871
318.15	0.6465	1101.824
318.15	0.7008	1102.351
318.15	0.7471	1102.727
318.15	0.7677	1102.876
318.15	0.8200	1103.216
318.15	0.8792	1103.548
318.15	0.8623	1103.458
318.15	0.8975	1103.642
318.15	0.9203	1103.756
318.15	0.9514	1103.905
318.15	0.9692	1103.989
318.15	1.0000	1104.132
323.15	0.0000	988.027
323.15	0.0107	999.177
323.15	0.0205	1008.259
323.15	0.0397	1023.558
323.15	0.0498	1030.371
323.15	0.0700	1041.993
323.15	0.0942	1053.042
323.15	0.1481	1069.567
323.15	0.2006	1079.068
323.15	0.2502	1084.728
323.15	0.2988	1088.448
323.15	0.3492	1091.154
323.15	0.3925	1092.875
323.15	0.4502	1094.607
323.15	0.4877	1095.484
323.15	0.5004	1095.747
323.15	0.5739	1097.006
323.15	0.5800	1097.094
323.15	0.6510	1097.964
323.15	0.6465	1097.916
323.15	0.7008	1098.445
323.15	0.7471	1098.821
323.15	0.7677	1098.971
323.15	0.8200	1099.312
323.15	0.8792	1099.645
323.15	0.8623	1099.555
323.15	0.8975	1099.74
323.15	0.9203	1099.853
323.15	0.9514	1100.001
323.15	0.9692	1100.084
323.15	1.0000	1100.224
328.15	0.0000	985.682
328.15	0.0107	996.693
328.15	0.0205	1005.638
328.15	0.0397	1020.667
328.15	0.0498	1027.35
328.15	0.0700	1038.742
328.15	0.0942	1049.576
328.15	0.1481	1065.819
328.15	0.2006	1075.203
328.15	0.2502	1080.818
328.15	0.2988	1084.517
328.15	0.3492	1087.214
328.15	0.3925	1088.933
328.15	0.4502	1090.665
328.15	0.4877	1091.545
328.15	0.5004	1091.809
328.15	0.5739	1093.076
328.15	0.5800	1093.165
328.15	0.6510	1094.043
328.15	0.6465	1093.995
328.15	0.7008	1094.529
328.15	0.7471	1094.908
328.15	0.7677	1095.059
328.15	0.8200	1095.401
328.15	0.8792	1095.733
328.15	0.8623	1095.643
328.15	0.8975	1095.826
328.15	0.9203	1095.938
328.15	0.9514	1096.085
328.15	0.9692	1096.166
328.15	1.0000	1096.304
333.15	0.0000	983.186
333.15	0.0107	994.065
333.15	0.0205	1002.886
333.15	0.0397	1017.675
333.15	0.0498	1024.24
333.15	0.0700	1035.424
333.15	0.0942	1046.055
333.15	0.1481	1062.017
333.15	0.2006	1071.276
333.15	0.2502	1076.844
333.15	0.2988	1080.531
333.15	0.3492	1083.23
333.15	0.3925	1084.955
333.15	0.4502	1086.697
333.15	0.4877	1087.583
333.15	0.5004	1087.849
333.15	0.5739	1089.126
333.15	0.5800	1089.215
333.15	0.6510	1090.101
333.15	0.6465	1090.053
333.15	0.7008	1090.592
333.15	0.7471	1090.974
333.15	0.7677	1091.127
333.15	0.8200	1091.471
333.15	0.8792	1091.805
333.15	0.8623	1091.715
333.15	0.8975	1091.9
333.15	0.9203	1092.012
333.15	0.9514	1092.159
333.15	0.9692	1092.241
333.15	1.0000	1092.378

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0101	1009.83
293.15	0.0196	1019.709
293.15	0.0290	1028.875
293.15	0.0381	1036.741
293.15	0.0496	1045.761
293.15	0.0601	1053.181
293.15	0.0689	1058.687
293.15	0.0801	1065.0
293.15	0.0905	1070.231
293.15	0.0996	1074.379
293.15	0.1479	1090.644
293.15	0.2004	1101.267
293.15	0.2462	1107.121
293.15	0.3004	1111.57
293.15	0.3474	1114.222
293.15	0.3948	1116.154
293.15	0.4467	1117.712
293.15	0.5021	1118.967
293.15	0.5480	1119.771
293.15	0.5923	1120.433
293.15	0.6442	1121.04
293.15	0.7095	1121.664
293.15	0.7531	1122.027
293.15	0.7859	1122.278
293.15	0.8387	1122.621
293.15	0.9031	1123.012
293.15	0.9181	1123.079
293.15	0.9344	1123.16
293.15	0.9569	1123.277
293.15	0.9782	1123.366
298.15	0.0101	1008.379
298.15	0.0196	1017.879
298.15	0.0290	1027.039
298.15	0.0381	1034.701
298.15	0.0496	1043.48
298.15	0.0601	1050.699
298.15	0.0689	1056.054
298.15	0.0801	1062.197
298.15	0.0905	1067.29
298.15	0.0996	1071.333
298.15	0.1479	1087.214
298.15	0.2004	1097.629
298.15	0.2462	1103.393
298.15	0.3004	1107.789
298.15	0.3474	1110.414
298.15	0.3948	1112.332
298.15	0.4467	1113.88
298.15	0.5021	1115.129
298.15	0.5480	1115.929
298.15	0.5923	1116.587
298.15	0.6442	1117.188
298.15	0.7095	1117.805
298.15	0.7531	1118.169
298.15	0.7859	1118.416
298.15	0.8387	1118.746
298.15	0.9031	1119.131
298.15	0.9181	1119.196
298.15	0.9344	1119.278
298.15	0.9569	1119.392
298.15	0.9782	1119.477
303.15	0.0101	1006.695
303.15	0.0196	1016.055
303.15	0.0290	1025.028
303.15	0.0381	1032.503
303.15	0.0496	1041.066
303.15	0.0601	1048.097
303.15	0.0689	1053.316
303.15	0.0801	1059.303
303.15	0.0905	1064.27
303.15	0.0996	1068.21
303.15	0.1479	1083.731
303.15	0.2004	1093.951
303.15	0.2462	1099.632
303.15	0.3004	1103.987
303.15	0.3474	1106.587
303.15	0.3948	1108.496
303.15	0.4467	1110.038
303.15	0.5021	1111.282
303.15	0.5480	1112.08
303.15	0.5923	1112.734
303.15	0.6442	1113.331
303.15	0.7095	1113.945
303.15	0.7531	1114.304
303.15	0.7859	1114.547
303.15	0.8387	1114.874
303.15	0.9031	1115.252
303.15	0.9181	1115.312
303.15	0.9344	1115.396
303.15	0.9569	1115.503
303.15	0.9782	1115.592
308.15	0.0101	1005.032
308.15	0.0196	1014.271
308.15	0.0290	1022.856
308.15	0.0381	1030.162
308.15	0.0496	1038.523
308.15	0.0601	1045.381
308.15	0.0689	1050.481
308.15	0.0801	1056.319
308.15	0.0905	1061.171
308.15	0.0996	1065.013
308.15	0.1479	1080.199
308.15	0.2004	1090.242
308.15	0.2462	1095.849
308.15	0.3004	1100.159
308.15	0.3474	1102.741
308.15	0.3948	1104.642
308.15	0.4467	1106.18
308.15	0.5021	1107.423
308.15	0.5480	1108.218
308.15	0.5923	1108.871
308.15	0.6442	1109.464
308.15	0.7095	1110.082
308.15	0.7531	1110.432
308.15	0.7859	1110.677
308.15	0.8387	1110.998
308.15	0.9031	1111.373
308.15	0.9181	1111.423
308.15	0.9344	1111.515
308.15	0.9569	1111.619
308.15	0.9782	1111.707
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	1123.477
298.15	1.0000	1119.586
303.15	1.0000	1115.703
308.15	1.0000	1111.814
293.15	0.0250	1024.911
293.15	0.0489	1044.887
293.15	0.0754	1062.235
293.15	0.0993	1074.348
293.15	0.1500	1091.94
293.15	0.1993	1101.822
293.15	0.2526	1107.939
293.15	0.2998	1111.261
293.15	0.3539	1113.94
293.15	0.4009	1115.826
293.15	0.4492	1117.526
293.15	0.4992	1119.037
293.15	0.5484	1120.205
293.15	0.5996	1121.027
293.15	0.6506	1121.459
293.15	0.7010	1121.616
293.15	0.7567	1121.705
293.15	0.8035	1121.913
293.15	0.8406	1122.247
293.15	0.8981	1123.022
293.15	0.9489	1123.572
298.15	0.0250	1023.095
298.15	0.0489	1042.583
298.15	0.0754	1059.509
298.15	0.0993	1071.331
298.15	0.1500	1088.51
298.15	0.1993	1098.179
298.15	0.2526	1104.187
298.15	0.2998	1107.47
298.15	0.3539	1110.13
298.15	0.4009	1112.009
298.15	0.4492	1113.702
298.15	0.4992	1115.204
298.15	0.5484	1116.361
298.15	0.5996	1117.175
298.15	0.6506	1117.601
298.15	0.7010	1117.756
298.15	0.7567	1117.845
298.15	0.8035	1118.05
298.15	0.8406	1118.38
298.15	0.8981	1119.145
298.15	0.9489	1119.685
303.15	0.0250	1021.124
303.15	0.0489	1040.158
303.15	0.0754	1056.69
303.15	0.0993	1068.238
303.15	0.1500	1085.03
303.15	0.1993	1094.498
303.15	0.2526	1100.405
303.15	0.2998	1103.652
303.15	0.3539	1106.301
303.15	0.4009	1108.177
303.15	0.4492	1109.867
303.15	0.4992	1111.363
303.15	0.5484	1112.514
303.15	0.5996	1113.319
303.15	0.6506	1113.74
303.15	0.7010	1113.891
303.15	0.7567	1113.977
303.15	0.8035	1114.181
303.15	0.8406	1114.508
303.15	0.8981	1115.265
303.15	0.9489	1115.798
308.15	0.0250	1019.054
308.15	0.0489	1037.636
308.15	0.0754	1053.782
308.15	0.0993	1065.065
308.15	0.1500	1081.49
308.15	0.1993	1090.776
308.15	0.2526	1096.597
308.15	0.2998	1099.817
308.15	0.3539	1102.458
308.15	0.4009	1104.332
308.15	0.4492	1106.018
308.15	0.4992	1107.509
308.15	0.5484	1108.652
308.15	0.5996	1109.451
308.15	0.6506	1109.869
308.15	0.7010	1110.021
308.15	0.7567	1110.109
308.15	0.8035	1110.313
308.15	0.8406	1110.638
308.15	0.8981	1111.387
308.15	0.9489	1111.911

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0965	1000.31
293.15	0.2002	1002.46
293.15	0.2920	1004.29
293.15	0.3986	1006.36
293.15	0.4988	1008.22
303.15	0.0965	997.73
303.15	0.2002	999.86
303.15	0.2920	1001.67
303.15	0.3986	1003.69
303.15	0.4988	1005.54
293.15	0.0000	998.21
303.15	0.0000	995.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0544	1001.214
278.15	0.1018	1002.295
278.15	0.2012	1004.531
278.15	0.3025	1006.774
278.15	0.4009	1008.917
283.15	0.0544	1000.922
283.15	0.1018	1001.977
283.15	0.2012	1004.153
283.15	0.3025	1006.338
283.15	0.4009	1008.423
288.15	0.0544	1000.298
288.15	0.1018	1001.329
288.15	0.2012	1003.456
288.15	0.3025	1005.59
288.15	0.4009	1007.625
293.15	0.0544	999.38
293.15	0.1018	1000.39
293.15	0.2012	1002.475
293.15	0.3025	1004.565
293.15	0.4009	1006.553
298.15	0.0544	998.2
298.15	0.1018	999.192
298.15	0.2012	1001.241
298.15	0.3025	1003.288
298.15	0.4009	1005.239
303.15	0.0544	996.785
303.15	0.1018	997.76
303.15	0.2012	999.776
303.15	0.3025	1001.787
303.15	0.4009	1003.7
308.15	0.0544	995.154
308.15	0.1018	996.109
308.15	0.2012	998.097
308.15	0.3025	1000.076
308.15	0.4009	1001.956
313.15	0.0544	993.322
313.15	0.1018	994.268
313.15	0.2012	996.223
313.15	0.3025	998.171
313.15	0.4009	1000.021
318.15	0.0544	991.307
318.15	0.1018	992.24
318.15	0.2012	994.166
318.15	0.3025	996.086
318.15	0.4009	997.909
323.15	0.0544	989.117
323.15	0.1018	990.037
323.15	0.2012	991.939
323.15	0.3025	993.832
323.15	0.4009	995.628
328.15	0.0544	986.763
328.15	0.1018	987.673
328.15	0.2012	989.548
328.15	0.3025	991.417
328.15	0.4009	993.188
333.15	0.0544	984.253
333.15	0.1018	985.152
333.15	0.2012	987.006
333.15	0.3025	988.85
333.15	0.4009	990.597
338.15	0.0544	981.597
338.15	0.1018	982.485
338.15	0.2012	984.316
338.15	0.3025	986.139
338.15	0.4009	987.864
343.15	0.0544	978.8
343.15	0.1018	979.677
343.15	0.2012	981.488
343.15	0.3025	983.288
343.15	0.4009	984.994

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0965	1001.366
288.15	0.2002	1003.551
288.15	0.2920	1005.416
288.15	0.3986	1007.496
288.15	0.4988	1009.367
288.15	0.5999	1011.202
288.15	0.6947	1012.819
288.15	0.7929	1014.471
298.15	0.0965	999.126
298.15	0.2002	1001.272
298.15	0.2920	1003.106
298.15	0.3986	1005.14
298.15	0.4988	1006.991
298.15	0.5999	1008.767
298.15	0.6947	1010.377
298.15	0.7929	1011.992
308.15	0.0965	996.095
308.15	0.2002	998.216
308.15	0.2920	1000.013
308.15	0.3986	1002.025
308.15	0.4988	1003.851
308.15	0.5999	1005.625
308.15	0.6947	1007.215
308.15	0.7929	1008.811
318.15	0.0965	992.405
318.15	0.2002	994.52
318.15	0.2920	996.322
318.15	0.3986	998.332
318.15	0.4988	1000.147
318.15	0.5999	1001.923
318.15	0.6947	1003.518
318.15	0.7929	1005.119

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Molality, mol/kg of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0965	293.15	1000.308
0.2002	293.15	1002.462
0.2920	293.15	1004.291
0.3986	293.15	1006.356
0.4988	293.15	1008.223
0.0965	298.15	999.126
0.2002	298.15	1001.272
0.2920	298.15	1003.106
0.3986	298.15	1005.14
0.4988	298.15	1006.991
0.0965	303.15	997.728
0.2002	303.15	999.858
0.2920	303.15	1001.668
0.3986	303.15	1003.693
0.4988	303.15	1005.54
0.0965	308.15	996.095
0.2002	308.15	998.216
0.2920	308.15	1000.013
0.3986	308.15	1002.025
0.4988	308.15	1003.851

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.2500	293.85	1108.0
0.2500	313.05	1093.0
0.2500	333.05	1078.0
0.2500	353.05	1061.0
0.2500	379.65	1039.0
0.2500	389.35	1030.0
0.2500	405.75	1016.0
0.2500	423.35	999.2
0.2500	442.45	980.0
0.5000	294.05	1120.0
0.5000	313.05	1105.0
0.5000	333.05	1089.0
0.5000	353.05	1073.0
0.5000	384.25	1046.0
0.5000	391.35	1041.0
0.5000	407.85	1028.0
0.5000	425.95	1011.0
0.5000	443.45	995.0
0.7500	294.15	1122.0
0.7500	313.05	1108.0
0.7500	333.05	1092.0
0.7500	353.05	1076.0
0.7500	384.95	1049.0
0.7500	392.55	1044.0
0.7500	407.45	1032.0
0.7500	425.35	1016.0
0.7500	444.55	999.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Triethylene glycol (1) - Liquid	Mass density, kg/m3 - Liquid
302.85	1.0000	1116.6
307.75	1.0000	1111.9
312.65	1.0000	1108.4
317.45	1.0000	1104.7
322.25	1.0000	1101.0
327.05	1.0000	1097.9
332.15	1.0000	1093.5
341.45	1.0000	1086.1
302.85	0.9100	1111.7
307.75	0.9100	1108.3
312.65	0.9100	1103.9
317.45	0.9100	1100.5
322.25	0.9100	1097.0
327.05	0.9100	1093.9
332.15	0.9100	1089.6
341.45	0.9100	1083.2
302.85	0.8200	1106.6
307.75	0.8200	1102.6
312.65	0.8200	1098.6
317.45	0.8200	1094.5
322.25	0.8200	1091.0
327.05	0.8200	1087.6
332.15	0.8200	1083.8
341.45	0.8200	1075.9
302.85	0.7200	1096.9
307.75	0.7200	1094.2
312.65	0.7200	1090.2
317.45	0.7200	1086.3
322.25	0.7200	1082.8
327.05	0.7200	1079.3
332.15	0.7200	1075.3
341.45	0.7200	1067.4

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0000	1466.57
288.15	0.0006	1469.72
288.15	0.0019	1476.6
288.15	0.0046	1490.1
288.15	0.0085	1508.91
288.15	0.0137	1531.96
288.15	0.0199	1557.66
288.15	0.0255	1578.73
288.15	0.0345	1609.12
288.15	0.0452	1639.86
288.15	0.0513	1655.19
288.15	0.0571	1668.33
288.15	0.0626	1679.51
288.15	0.0692	1691.55
288.15	0.0742	1699.8
288.15	0.0802	1708.53
288.15	0.0843	1714.09
288.15	0.0883	1718.97
288.15	0.0930	1724.16
288.15	0.0966	1727.82
288.15	0.1007	1731.65
288.15	0.1021	1732.93
288.15	0.1045	1734.93
288.15	0.1091	1738.42
288.15	0.1208	1745.68
288.15	0.1237	1747.17
288.15	0.1281	1749.1
288.15	0.1302	1749.97
288.15	0.1330	1751.0
288.15	0.1394	1753.0
288.15	0.1441	1754.18
288.15	0.1474	1754.85
288.15	0.1578	1756.29
288.15	0.1678	1756.83
288.15	0.1774	1756.69
288.15	0.1904	1755.66
288.15	0.2055	1753.54
288.15	0.2329	1748.03
288.15	0.2559	1742.46
288.15	0.2967	1731.94
288.15	0.3235	1725.13
288.15	0.3699	1713.95
288.15	0.4089	1705.23
288.15	0.5029	1686.53
288.15	0.6337	1666.99
288.15	0.7450	1657.94
288.15	0.8795	1649.62
288.15	0.9612	1645.87
288.15	1.0000	1643.87
293.15	0.0000	1482.33
293.15	0.0007	1485.61
293.15	0.0025	1494.05
293.15	0.0050	1505.7
293.15	0.0078	1518.0
293.15	0.0146	1546.14
293.15	0.0204	1567.92
293.15	0.0276	1592.12
293.15	0.0328	1607.98
293.15	0.0418	1632.72
293.15	0.0490	1649.89
293.15	0.0556	1663.96
293.15	0.0631	1678.05
293.15	0.0678	1685.81
293.15	0.0736	1694.57
293.15	0.0816	1705.12
293.15	0.0889	1713.25
293.15	0.0970	1720.97
293.15	0.1043	1726.72
293.15	0.1091	1729.95
293.15	0.1142	1732.95
293.15	0.1200	1735.86
293.15	0.1325	1740.59
293.15	0.1374	1741.89
293.15	0.1445	1743.33
293.15	0.1752	1744.61
293.15	0.1869	1743.52
293.15	0.2052	1740.69
293.15	0.2239	1736.78
293.15	0.2513	1730.09
293.15	0.2755	1723.74
293.15	0.3023	1716.72
293.15	0.3754	1699.0
293.15	0.4338	1686.56
293.15	0.5151	1671.3
293.15	0.6233	1654.89
293.15	0.7815	1641.21
293.15	0.8924	1634.67
293.15	0.9634	1630.17
293.15	1.0000	1629.02
298.15	0.0000	1496.75
298.15	0.0007	1499.65
298.15	0.0031	1510.18
298.15	0.0087	1533.11
298.15	0.0151	1557.0
298.15	0.0205	1575.41
298.15	0.0297	1603.31
298.15	0.0382	1625.65
298.15	0.0453	1642.08
298.15	0.0511	1654.09
298.15	0.0584	1667.62
298.15	0.0674	1681.9
298.15	0.0766	1694.09
298.15	0.0827	1700.97
298.15	0.0888	1707.02
298.15	0.0957	1712.89
298.15	0.1024	1717.71
298.15	0.1041	1718.83
298.15	0.1099	1722.19
298.15	0.1152	1724.84
298.15	0.1205	1727.04
298.15	0.1270	1729.27
298.15	0.1291	1729.87
298.15	0.1383	1731.91
298.15	0.1474	1733.12
298.15	0.1587	1733.65
298.15	0.1675	1733.43
298.15	0.1757	1732.82
298.15	0.1834	1731.93
298.15	0.2026	1728.7
298.15	0.2210	1724.65
298.15	0.2393	1720.07
298.15	0.2566	1715.47
298.15	0.2906	1706.3
298.15	0.3533	1690.45
298.15	0.4270	1674.41
298.15	0.5126	1658.34
298.15	0.5907	1645.69
298.15	0.7663	1627.21
298.15	0.8917	1620.05
298.15	0.9628	1615.59
298.15	1.0000	1613.52
303.15	0.0000	1509.39
303.15	0.0010	1513.45
303.15	0.0028	1520.42
303.15	0.0079	1539.9
303.15	0.0112	1551.54
303.15	0.0191	1577.02
303.15	0.0244	1592.62
303.15	0.0326	1614.28
303.15	0.0428	1637.25
303.15	0.0507	1652.47
303.15	0.0579	1664.66
303.15	0.0662	1676.76
303.15	0.0743	1686.64
303.15	0.0818	1694.52
303.15	0.0889	1700.8
303.15	0.0936	1704.45
303.15	0.0985	1707.81
303.15	0.1020	1709.94
303.15	0.1059	1712.06
303.15	0.1101	1714.12
303.15	0.1102	1714.16
303.15	0.1147	1716.04
303.15	0.1193	1717.72
303.15	0.1248	1719.35
303.15	0.1295	1720.48
303.15	0.1308	1720.74
303.15	0.1337	1721.28
303.15	0.1393	1722.07
303.15	0.1423	1722.38
303.15	0.1457	1722.64
303.15	0.1695	1722.1
303.15	0.1857	1719.93
303.15	0.2042	1716.31
303.15	0.2252	1711.22
303.15	0.2499	1704.57
303.15	0.3027	1690.03
303.15	0.3394	1680.59
303.15	0.4052	1665.69
303.15	0.4916	1648.96
303.15	0.6074	1630.04
303.15	0.7552	1614.03
303.15	0.8683	1607.4
303.15	0.9616	1601.73
303.15	1.0000	1599.09
308.15	0.0000	1520.13
308.15	0.0007	1522.75
308.15	0.0022	1528.13
308.15	0.0057	1540.62
308.15	0.0104	1555.97
308.15	0.0151	1570.69
308.15	0.0239	1595.0
308.15	0.0318	1614.13
308.15	0.0428	1636.97
308.15	0.0506	1650.6
308.15	0.0579	1661.85
308.15	0.0645	1670.56
308.15	0.0734	1680.77
308.15	0.0834	1690.02
308.15	0.0908	1695.55
308.15	0.1028	1702.57
308.15	0.1137	1707.08
308.15	0.1189	1708.66
308.15	0.1229	1709.65
308.15	0.1231	1709.69
308.15	0.1269	1710.47
308.15	0.1308	1711.13
308.15	0.1403	1712.1
308.15	0.1427	1712.23
308.15	0.1481	1712.34
308.15	0.1594	1711.92
308.15	0.1659	1711.33
308.15	0.1738	1710.33
308.15	0.1858	1708.29
308.15	0.1969	1705.97
308.15	0.2172	1700.99
308.15	0.2467	1692.82
308.15	0.2825	1682.6
308.15	0.3259	1670.84
308.15	0.3691	1660.32
308.15	0.4352	1646.18
308.15	0.5067	1632.73
308.15	0.6111	1615.94
308.15	0.7783	1598.52
308.15	0.8912	1591.89
308.15	0.9608	1587.47
308.15	1.0000	1584.59
313.15	0.0000	1528.82
313.15	0.0006	1530.83
313.15	0.0027	1537.87
313.15	0.0069	1551.19
313.15	0.0101	1560.8
313.15	0.0149	1574.65
313.15	0.0227	1594.64
313.15	0.0298	1610.68
313.15	0.0358	1623.0
313.15	0.0422	1634.61
313.15	0.0504	1647.85
313.15	0.0569	1656.84
313.15	0.0669	1668.66
313.15	0.0769	1678.28
313.15	0.0829	1683.0
313.15	0.0913	1688.6
313.15	0.0926	1689.34
313.15	0.1004	1693.29
313.15	0.1079	1696.25
313.15	0.1160	1698.65
313.15	0.1201	1699.58
313.15	0.1232	1700.16
313.15	0.1303	1701.12
313.15	0.1343	1701.45
313.15	0.1377	1701.63
313.15	0.1423	1701.73
313.15	0.1573	1701.02
313.15	0.1723	1699.02
313.15	0.1866	1696.25
313.15	0.2037	1692.18
313.15	0.2426	1681.2
313.15	0.2794	1670.28
313.15	0.3209	1658.64
313.15	0.4030	1638.82
313.15	0.4658	1625.95
313.15	0.5676	1607.97
313.15	0.6969	1590.84
313.15	0.8694	1577.89
313.15	0.9455	1572.88
313.15	1.0000	1569.06
318.15	0.0000	1536.65
318.15	0.0006	1538.49
318.15	0.0020	1542.89
318.15	0.0044	1550.01
318.15	0.0103	1566.63
318.15	0.0148	1578.51
318.15	0.0207	1592.58
318.15	0.0282	1608.63
318.15	0.0344	1620.53
318.15	0.0436	1635.91
318.15	0.0515	1647.09
318.15	0.0590	1656.38
318.15	0.0657	1663.43
318.15	0.0730	1670.03
318.15	0.0829	1677.38
318.15	0.0913	1682.21
318.15	0.0966	1684.75
318.15	0.1018	1686.82
318.15	0.1056	1688.11
318.15	0.1135	1690.24
318.15	0.1255	1692.17
318.15	0.1394	1692.76
318.15	0.1396	1692.76
318.15	0.1432	1692.67
318.15	0.1521	1692.08
318.15	0.1731	1689.02
318.15	0.1931	1684.53
318.15	0.2076	1680.67
318.15	0.2511	1667.71
318.15	0.3044	1651.81
318.15	0.3572	1637.68
318.15	0.4142	1624.42
318.15	0.4989	1607.59
318.15	0.6427	1585.52
318.15	0.7971	1571.28
318.15	0.8865	1565.06
318.15	0.9641	1559.61
318.15	1.0000	1554.68

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 Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0101	1526.71
293.15	0.0196	1563.29
293.15	0.0290	1595.66
293.15	0.0381	1622.51
293.15	0.0496	1651.61
293.15	0.0601	1673.75
293.15	0.0689	1688.96
293.15	0.0801	1704.87
293.15	0.0905	1716.55
293.15	0.0996	1724.68
293.15	0.1479	1744.45
293.15	0.2004	1742.02
293.15	0.2462	1732.13
293.15	0.3004	1718.19
293.15	0.3474	1706.1
293.15	0.3948	1694.85
293.15	0.4467	1683.86
293.15	0.5021	1673.62
293.15	0.5480	1666.35
293.15	0.5923	1659.96
293.15	0.6442	1653.73
293.15	0.7095	1647.03
293.15	0.7531	1642.92
293.15	0.7859	1640.18
293.15	0.8387	1636.46
293.15	0.9031	1632.06
293.15	0.9181	1631.35
293.15	0.9344	1630.51
293.15	0.9569	1629.23
293.15	0.9782	1628.12
298.15	0.0101	1537.44
298.15	0.0196	1570.95
298.15	0.0290	1600.5
298.15	0.0381	1624.97
298.15	0.0496	1651.38
298.15	0.0601	1671.44
298.15	0.0689	1685.1
298.15	0.0801	1699.36
298.15	0.0905	1709.75
298.15	0.0996	1716.92
298.15	0.1479	1733.38
298.15	0.2004	1729.33
298.15	0.2462	1718.76
298.15	0.3004	1704.42
298.15	0.3474	1692.09
298.15	0.3948	1680.7
298.15	0.4467	1669.58
298.15	0.5021	1659.23
298.15	0.5480	1651.87
298.15	0.5923	1645.4
298.15	0.6442	1639.08
298.15	0.7095	1632.31
298.15	0.7531	1628.13
298.15	0.7859	1625.31
298.15	0.8387	1621.47
298.15	0.9031	1616.97
298.15	0.9181	1616.25
298.15	0.9344	1615.38
298.15	0.9569	1614.07
298.15	0.9782	1612.93
303.15	0.0101	1546.56
303.15	0.0196	1577.25
303.15	0.0290	1604.22
303.15	0.0381	1626.45
303.15	0.0496	1650.37
303.15	0.0601	1668.44
303.15	0.0689	1680.68
303.15	0.0801	1693.39
303.15	0.0905	1702.55
303.15	0.0996	1708.81
303.15	0.1479	1722.14
303.15	0.2004	1716.55
303.15	0.2462	1705.34
303.15	0.3004	1690.62
303.15	0.3474	1678.1
303.15	0.3948	1666.59
303.15	0.4467	1655.37
303.15	0.5021	1644.92
303.15	0.5480	1637.48
303.15	0.5923	1630.95
303.15	0.6442	1624.53
303.15	0.7095	1617.7
303.15	0.7531	1613.4
303.15	0.7859	1610.53
303.15	0.8387	1606.6
303.15	0.9031	1602.0
303.15	0.9181	1601.26
303.15	0.9344	1600.37
303.15	0.9569	1599.04
303.15	0.9782	1597.88
308.15	0.0101	1554.15
308.15	0.0196	1582.25
308.15	0.0290	1606.81
308.15	0.0381	1626.99
308.15	0.0496	1648.59
308.15	0.0601	1664.8
308.15	0.0689	1675.75
308.15	0.0801	1686.96
308.15	0.0905	1694.97
308.15	0.0996	1700.36
308.15	0.1479	1710.76
308.15	0.2004	1703.72
308.15	0.2462	1691.91
308.15	0.3004	1676.84
308.15	0.3474	1664.16
308.15	0.3948	1652.54
308.15	0.4467	1641.23
308.15	0.5021	1630.7
308.15	0.5480	1623.22
308.15	0.5923	1616.64
308.15	0.6442	1610.11
308.15	0.7095	1603.23
308.15	0.7531	1598.82
308.15	0.7859	1595.9
308.15	0.8387	1591.88
308.15	0.9031	1587.2
308.15	0.9181	1586.45
308.15	0.9344	1585.54
308.15	0.9569	1584.19
308.15	0.9782	1582.99
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	1626.77
298.15	1.0000	1611.61
303.15	1.0000	1596.57
308.15	1.0000	1581.69

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 Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0965	1489.9
293.15	0.2002	1498.0
293.15	0.2920	1504.8
293.15	0.3986	1513.1
293.15	0.4988	1520.5
303.15	0.0965	1514.9
303.15	0.2002	1521.8
303.15	0.2920	1528.0
303.15	0.3986	1535.1
303.15	0.4988	1541.7
293.15	0.0000	1482.3
303.15	0.0000	1508.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
278.15	0.0544	1432.02
278.15	0.1018	1436.73
278.15	0.2012	1447.42
278.15	0.3025	1457.55
278.15	0.4009	1467.09
283.15	0.0544	1452.54
283.15	0.1018	1456.92
283.15	0.2012	1466.65
283.15	0.3025	1475.96
283.15	0.4009	1484.76
288.15	0.0544	1470.81
288.15	0.1018	1474.88
288.15	0.2012	1483.73
288.15	0.3025	1492.31
288.15	0.4009	1500.42
293.15	0.0544	1486.86
293.15	0.1018	1490.64
293.15	0.2012	1498.77
293.15	0.3025	1506.63
293.15	0.4009	1514.13
298.15	0.0544	1500.95
298.15	0.1018	1504.46
298.15	0.2012	1511.85
298.15	0.3025	1519.15
298.15	0.4009	1526.01
303.15	0.0544	1513.13
303.15	0.1018	1516.4
303.15	0.2012	1523.13
303.15	0.3025	1529.86
303.15	0.4009	1536.23
308.15	0.0544	1523.55
308.15	0.1018	1526.61
308.15	0.2012	1532.75
308.15	0.3025	1538.97
308.15	0.4009	1544.84
313.15	0.0544	1532.37
313.15	0.1018	1535.08
313.15	0.2012	1540.85
313.15	0.3025	1546.57
313.15	0.4009	1551.93
318.15	0.0544	1539.71
318.15	0.1018	1542.17
318.15	0.2012	1547.5
318.15	0.3025	1552.73
318.15	0.4009	1557.65
323.15	0.0544	1545.64
323.15	0.1018	1547.9
323.15	0.2012	1552.76
323.15	0.3025	1557.55
323.15	0.4009	1562.05
328.15	0.0544	1550.24
328.15	0.1018	1552.32
328.15	0.2012	1556.74
328.15	0.3025	1561.12
328.15	0.4009	1565.22
333.15	0.0544	1553.61
333.15	0.1018	1555.5
333.15	0.2012	1559.53
333.15	0.3025	1563.51
333.15	0.4009	1567.26
338.15	0.0544	1555.83
338.15	0.1018	1557.54
338.15	0.2012	1561.19
338.15	0.3025	1564.81
338.15	0.4009	1568.19
343.15	0.0544	1556.98
343.15	0.1018	1558.51
343.15	0.2012	1561.81
343.15	0.3025	1565.08
343.15	0.4009	1568.12

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 Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0965	1474.72
288.15	0.2002	1483.26
288.15	0.2920	1491.74
288.15	0.3986	1499.22
288.15	0.4988	1508.48
288.15	0.5999	1516.07
288.15	0.6947	1523.59
288.15	0.7929	1531.19
298.15	0.0965	1503.48
298.15	0.2002	1511.04
298.15	0.2920	1517.62
298.15	0.3986	1525.38
298.15	0.4988	1532.21
298.15	0.5999	1542.37
298.15	0.6947	1551.24
298.15	0.7929	1560.56
308.15	0.0965	1525.09
308.15	0.2002	1531.28
308.15	0.2920	1536.87
308.15	0.3986	1543.31
308.15	0.4988	1550.94
308.15	0.5999	1563.23
308.15	0.6947	1572.72
308.15	0.7929	1582.65
318.15	0.0965	1543.95
318.15	0.2002	1552.21
318.15	0.2920	1560.57
318.15	0.3986	1567.78
318.15	0.4988	1576.89
318.15	0.5999	1584.48
318.15	0.6947	1592.31
318.15	0.7929	1600.48

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Molality, mol/kg of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0965	293.15	1489.87
0.2002	293.15	1498.03
0.2920	293.15	1504.81
0.3986	293.15	1513.14
0.4988	293.15	1520.51
0.0965	298.15	1503.48
0.2002	298.15	1511.04
0.2920	298.15	1517.62
0.3986	298.15	1525.38
0.4988	298.15	1532.21
0.0965	303.15	1514.85
0.2002	303.15	1521.76
0.2920	303.15	1528.02
0.3986	303.15	1535.06
0.4988	303.15	1541.68
0.0965	308.15	1525.09
0.2002	308.15	1531.28
0.2920	308.15	1536.87
0.3986	308.15	1543.31
0.4988	308.15	1549.44

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0000	1466.57
288.15	0.0006	1469.72
288.15	0.0019	1476.6
288.15	0.0046	1490.1
288.15	0.0085	1508.91
288.15	0.0137	1531.96
288.15	0.0199	1557.66
288.15	0.0255	1578.73
288.15	0.0345	1609.12
288.15	0.0452	1639.86
288.15	0.0513	1655.19
288.15	0.0571	1668.33
288.15	0.0626	1679.51
288.15	0.0692	1691.55
288.15	0.0742	1699.8
288.15	0.0802	1708.53
288.15	0.0843	1714.09
288.15	0.0883	1718.97
288.15	0.0930	1724.16
288.15	0.0966	1727.82
288.15	0.1007	1731.65
288.15	0.1021	1732.93
288.15	0.1045	1734.93
288.15	0.1091	1738.42
288.15	0.1208	1745.68
288.15	0.1237	1747.17
288.15	0.1281	1749.1
288.15	0.1302	1749.97
288.15	0.1330	1751.0
288.15	0.1394	1753.0
288.15	0.1441	1754.18
288.15	0.1474	1754.85
288.15	0.1578	1756.29
288.15	0.1678	1756.83
288.15	0.1774	1756.69
288.15	0.1904	1755.66
288.15	0.2055	1753.54
288.15	0.2329	1748.03
288.15	0.2559	1742.46
288.15	0.2967	1731.94
288.15	0.3235	1725.13
288.15	0.3699	1713.95
288.15	0.4089	1705.23
288.15	0.5029	1686.53
288.15	0.6337	1666.99
288.15	0.7450	1657.94
288.15	0.8795	1649.62
288.15	0.9612	1645.87
288.15	1.0000	1643.87
293.15	0.0000	1482.33
293.15	0.0007	1485.61
293.15	0.0025	1494.05
293.15	0.0050	1505.7
293.15	0.0078	1518.0
293.15	0.0146	1546.14
293.15	0.0204	1567.92
293.15	0.0276	1592.12
293.15	0.0328	1607.98
293.15	0.0418	1632.72
293.15	0.0490	1649.89
293.15	0.0556	1663.96
293.15	0.0631	1678.05
293.15	0.0678	1685.81
293.15	0.0736	1694.57
293.15	0.0816	1705.12
293.15	0.0889	1713.25
293.15	0.0970	1720.97
293.15	0.1043	1726.72
293.15	0.1091	1729.95
293.15	0.1142	1732.95
293.15	0.1200	1735.86
293.15	0.1325	1740.59
293.15	0.1374	1741.89
293.15	0.1445	1743.33
293.15	0.1752	1744.61
293.15	0.1869	1743.52
293.15	0.2052	1740.69
293.15	0.2239	1736.78
293.15	0.2513	1730.09
293.15	0.2755	1723.74
293.15	0.3023	1716.72
293.15	0.3754	1699.0
293.15	0.4338	1686.56
293.15	0.5151	1671.3
293.15	0.6233	1654.89
293.15	0.7815	1641.21
293.15	0.8924	1634.67
293.15	0.9634	1630.17
293.15	1.0000	1629.02
298.15	0.0000	1496.75
298.15	0.0007	1499.65
298.15	0.0031	1510.18
298.15	0.0087	1533.11
298.15	0.0151	1557.0
298.15	0.0205	1575.41
298.15	0.0297	1603.31
298.15	0.0382	1625.65
298.15	0.0453	1642.08
298.15	0.0511	1654.09
298.15	0.0584	1667.62
298.15	0.0674	1681.9
298.15	0.0766	1694.09
298.15	0.0827	1700.97
298.15	0.0888	1707.02
298.15	0.0957	1712.89
298.15	0.1024	1717.71
298.15	0.1041	1718.83
298.15	0.1099	1722.19
298.15	0.1152	1724.84
298.15	0.1205	1727.04
298.15	0.1270	1729.27
298.15	0.1291	1729.87
298.15	0.1383	1731.91
298.15	0.1474	1733.12
298.15	0.1587	1733.65
298.15	0.1675	1733.43
298.15	0.1757	1732.82
298.15	0.1834	1731.93
298.15	0.2026	1728.7
298.15	0.2210	1724.65
298.15	0.2393	1720.07
298.15	0.2566	1715.47
298.15	0.2906	1706.3
298.15	0.3533	1690.45
298.15	0.4270	1674.41
298.15	0.5126	1658.34
298.15	0.5907	1645.69
298.15	0.7663	1627.21
298.15	0.8917	1620.05
298.15	0.9628	1615.59
298.15	1.0000	1613.52
303.15	0.0000	1509.39
303.15	0.0010	1513.45
303.15	0.0028	1520.42
303.15	0.0079	1539.9
303.15	0.0112	1551.54
303.15	0.0191	1577.02
303.15	0.0244	1592.62
303.15	0.0326	1614.28
303.15	0.0428	1637.25
303.15	0.0507	1652.47
303.15	0.0579	1664.66
303.15	0.0662	1676.76
303.15	0.0743	1686.64
303.15	0.0818	1694.52
303.15	0.0889	1700.8
303.15	0.0936	1704.45
303.15	0.0985	1707.81
303.15	0.1020	1709.94
303.15	0.1059	1712.06
303.15	0.1101	1714.12
303.15	0.1102	1714.16
303.15	0.1147	1716.04
303.15	0.1193	1717.72
303.15	0.1248	1719.35
303.15	0.1295	1720.48
303.15	0.1308	1720.74
303.15	0.1337	1721.28
303.15	0.1393	1722.07
303.15	0.1423	1722.38
303.15	0.1457	1722.64
303.15	0.1695	1722.1
303.15	0.1857	1719.93
303.15	0.2042	1716.31
303.15	0.2252	1711.22
303.15	0.2499	1704.57
303.15	0.3027	1690.03
303.15	0.3394	1680.59
303.15	0.4052	1665.69
303.15	0.4916	1648.96
303.15	0.6074	1630.04
303.15	0.7552	1614.03
303.15	0.8683	1607.4
303.15	0.9616	1601.73
303.15	1.0000	1599.09
308.15	0.0000	1520.13
308.15	0.0007	1522.75
308.15	0.0022	1528.13
308.15	0.0057	1540.62
308.15	0.0104	1555.97
308.15	0.0151	1570.69
308.15	0.0239	1595.0
308.15	0.0318	1614.13
308.15	0.0428	1636.97
308.15	0.0506	1650.6
308.15	0.0579	1661.85
308.15	0.0645	1670.56
308.15	0.0734	1680.77
308.15	0.0834	1690.02
308.15	0.0908	1695.55
308.15	0.1028	1702.57
308.15	0.1137	1707.08
308.15	0.1189	1708.66
308.15	0.1229	1709.65
308.15	0.1231	1709.69
308.15	0.1269	1710.47
308.15	0.1308	1711.13
308.15	0.1403	1712.1
308.15	0.1427	1712.23
308.15	0.1481	1712.34
308.15	0.1594	1711.92
308.15	0.1659	1711.33
308.15	0.1738	1710.33
308.15	0.1858	1708.29
308.15	0.1969	1705.97
308.15	0.2172	1700.99
308.15	0.2467	1692.82
308.15	0.2825	1682.6
308.15	0.3259	1670.84
308.15	0.3691	1660.32
308.15	0.4352	1646.18
308.15	0.5067	1632.73
308.15	0.6111	1615.94
308.15	0.7783	1598.52
308.15	0.8912	1591.89
308.15	0.9608	1587.47
308.15	1.0000	1584.59
313.15	0.0000	1528.82
313.15	0.0006	1530.83
313.15	0.0027	1537.87
313.15	0.0069	1551.19
313.15	0.0101	1560.8
313.15	0.0149	1574.65
313.15	0.0227	1594.64
313.15	0.0298	1610.68
313.15	0.0358	1623.0
313.15	0.0422	1634.61
313.15	0.0504	1647.85
313.15	0.0569	1656.84
313.15	0.0669	1668.66
313.15	0.0769	1678.28
313.15	0.0829	1683.0
313.15	0.0913	1688.6
313.15	0.0926	1689.34
313.15	0.1004	1693.29
313.15	0.1079	1696.25
313.15	0.1160	1698.65
313.15	0.1201	1699.58
313.15	0.1232	1700.16
313.15	0.1303	1701.12
313.15	0.1343	1701.45
313.15	0.1377	1701.63
313.15	0.1423	1701.73
313.15	0.1573	1701.02
313.15	0.1723	1699.02
313.15	0.1866	1696.25
313.15	0.2037	1692.18
313.15	0.2426	1681.2
313.15	0.2794	1670.28
313.15	0.3209	1658.64
313.15	0.4030	1638.82
313.15	0.4658	1625.95
313.15	0.5676	1607.97
313.15	0.6969	1590.84
313.15	0.8694	1577.89
313.15	0.9455	1572.88
313.15	1.0000	1569.06
318.15	0.0000	1536.65
318.15	0.0006	1538.49
318.15	0.0020	1542.89
318.15	0.0044	1550.01
318.15	0.0103	1566.63
318.15	0.0148	1578.51
318.15	0.0207	1592.58
318.15	0.0282	1608.63
318.15	0.0344	1620.53
318.15	0.0436	1635.91
318.15	0.0515	1647.09
318.15	0.0590	1656.38
318.15	0.0657	1663.43
318.15	0.0730	1670.03
318.15	0.0829	1677.38
318.15	0.0913	1682.21
318.15	0.0966	1684.75
318.15	0.1018	1686.82
318.15	0.1056	1688.11
318.15	0.1135	1690.24
318.15	0.1255	1692.17
318.15	0.1394	1692.76
318.15	0.1396	1692.76
318.15	0.1432	1692.67
318.15	0.1521	1692.08
318.15	0.1731	1689.02
318.15	0.1931	1684.53
318.15	0.2076	1680.67
318.15	0.2511	1667.71
318.15	0.3044	1651.81
318.15	0.3572	1637.68
318.15	0.4142	1624.42
318.15	0.4989	1607.59
318.15	0.6427	1585.52
318.15	0.7971	1571.28
318.15	0.8865	1565.06
318.15	0.9641	1559.61
318.15	1.0000	1554.68

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 Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0101	1526.71
293.15	0.0196	1563.29
293.15	0.0290	1595.66
293.15	0.0381	1622.51
293.15	0.0496	1651.61
293.15	0.0601	1673.75
293.15	0.0689	1688.96
293.15	0.0801	1704.87
293.15	0.0905	1716.55
293.15	0.0996	1724.68
293.15	0.1479	1744.45
293.15	0.2004	1742.02
293.15	0.2462	1732.13
293.15	0.3004	1718.19
293.15	0.3474	1706.1
293.15	0.3948	1694.85
293.15	0.4467	1683.86
293.15	0.5021	1673.62
293.15	0.5480	1666.35
293.15	0.5923	1659.96
293.15	0.6442	1653.73
293.15	0.7095	1647.03
293.15	0.7531	1642.92
293.15	0.7859	1640.18
293.15	0.8387	1636.46
293.15	0.9031	1632.06
293.15	0.9181	1631.35
293.15	0.9344	1630.51
293.15	0.9569	1629.23
293.15	0.9782	1628.12
298.15	0.0101	1537.44
298.15	0.0196	1570.95
298.15	0.0290	1600.5
298.15	0.0381	1624.97
298.15	0.0496	1651.38
298.15	0.0601	1671.44
298.15	0.0689	1685.1
298.15	0.0801	1699.36
298.15	0.0905	1709.75
298.15	0.0996	1716.92
298.15	0.1479	1733.38
298.15	0.2004	1729.33
298.15	0.2462	1718.76
298.15	0.3004	1704.42
298.15	0.3474	1692.09
298.15	0.3948	1680.7
298.15	0.4467	1669.58
298.15	0.5021	1659.23
298.15	0.5480	1651.87
298.15	0.5923	1645.4
298.15	0.6442	1639.08
298.15	0.7095	1632.31
298.15	0.7531	1628.13
298.15	0.7859	1625.31
298.15	0.8387	1621.47
298.15	0.9031	1616.97
298.15	0.9181	1616.25
298.15	0.9344	1615.38
298.15	0.9569	1614.07
298.15	0.9782	1612.93
303.15	0.0101	1546.56
303.15	0.0196	1577.25
303.15	0.0290	1604.22
303.15	0.0381	1626.45
303.15	0.0496	1650.37
303.15	0.0601	1668.44
303.15	0.0689	1680.68
303.15	0.0801	1693.39
303.15	0.0905	1702.55
303.15	0.0996	1708.81
303.15	0.1479	1722.14
303.15	0.2004	1716.55
303.15	0.2462	1705.34
303.15	0.3004	1690.62
303.15	0.3474	1678.1
303.15	0.3948	1666.59
303.15	0.4467	1655.37
303.15	0.5021	1644.92
303.15	0.5480	1637.48
303.15	0.5923	1630.95
303.15	0.6442	1624.53
303.15	0.7095	1617.7
303.15	0.7531	1613.4
303.15	0.7859	1610.53
303.15	0.8387	1606.6
303.15	0.9031	1602.0
303.15	0.9181	1601.26
303.15	0.9344	1600.37
303.15	0.9569	1599.04
303.15	0.9782	1597.88
308.15	0.0101	1554.15
308.15	0.0196	1582.25
308.15	0.0290	1606.81
308.15	0.0381	1626.99
308.15	0.0496	1648.59
308.15	0.0601	1664.8
308.15	0.0689	1675.75
308.15	0.0801	1686.96
308.15	0.0905	1694.97
308.15	0.0996	1700.36
308.15	0.1479	1710.76
308.15	0.2004	1703.72
308.15	0.2462	1691.91
308.15	0.3004	1676.84
308.15	0.3474	1664.16
308.15	0.3948	1652.54
308.15	0.4467	1641.23
308.15	0.5021	1630.7
308.15	0.5480	1623.22
308.15	0.5923	1616.64
308.15	0.6442	1610.11
308.15	0.7095	1603.23
308.15	0.7531	1598.82
308.15	0.7859	1595.9
308.15	0.8387	1591.88
308.15	0.9031	1587.2
308.15	0.9181	1586.45
308.15	0.9344	1585.54
308.15	0.9569	1584.19
308.15	0.9782	1582.99
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	1626.77
298.15	1.0000	1611.61
303.15	1.0000	1596.57
308.15	1.0000	1581.69

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 Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0965	1489.9
293.15	0.2002	1498.0
293.15	0.2920	1504.8
293.15	0.3986	1513.1
293.15	0.4988	1520.5
303.15	0.0965	1514.9
303.15	0.2002	1521.8
303.15	0.2920	1528.0
303.15	0.3986	1535.1
303.15	0.4988	1541.7
293.15	0.0000	1482.3
303.15	0.0000	1508.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
278.15	0.0544	1432.02
278.15	0.1018	1436.73
278.15	0.2012	1447.42
278.15	0.3025	1457.55
278.15	0.4009	1467.09
283.15	0.0544	1452.54
283.15	0.1018	1456.92
283.15	0.2012	1466.65
283.15	0.3025	1475.96
283.15	0.4009	1484.76
288.15	0.0544	1470.81
288.15	0.1018	1474.88
288.15	0.2012	1483.73
288.15	0.3025	1492.31
288.15	0.4009	1500.42
293.15	0.0544	1486.86
293.15	0.1018	1490.64
293.15	0.2012	1498.77
293.15	0.3025	1506.63
293.15	0.4009	1514.13
298.15	0.0544	1500.95
298.15	0.1018	1504.46
298.15	0.2012	1511.85
298.15	0.3025	1519.15
298.15	0.4009	1526.01
303.15	0.0544	1513.13
303.15	0.1018	1516.4
303.15	0.2012	1523.13
303.15	0.3025	1529.86
303.15	0.4009	1536.23
308.15	0.0544	1523.55
308.15	0.1018	1526.61
308.15	0.2012	1532.75
308.15	0.3025	1538.97
308.15	0.4009	1544.84
313.15	0.0544	1532.37
313.15	0.1018	1535.08
313.15	0.2012	1540.85
313.15	0.3025	1546.57
313.15	0.4009	1551.93
318.15	0.0544	1539.71
318.15	0.1018	1542.17
318.15	0.2012	1547.5
318.15	0.3025	1552.73
318.15	0.4009	1557.65
323.15	0.0544	1545.64
323.15	0.1018	1547.9
323.15	0.2012	1552.76
323.15	0.3025	1557.55
323.15	0.4009	1562.05
328.15	0.0544	1550.24
328.15	0.1018	1552.32
328.15	0.2012	1556.74
328.15	0.3025	1561.12
328.15	0.4009	1565.22
333.15	0.0544	1553.61
333.15	0.1018	1555.5
333.15	0.2012	1559.53
333.15	0.3025	1563.51
333.15	0.4009	1567.26
338.15	0.0544	1555.83
338.15	0.1018	1557.54
338.15	0.2012	1561.19
338.15	0.3025	1564.81
338.15	0.4009	1568.19
343.15	0.0544	1556.98
343.15	0.1018	1558.51
343.15	0.2012	1561.81
343.15	0.3025	1565.08
343.15	0.4009	1568.12

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 Triethylene glycol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0965	1474.72
288.15	0.2002	1483.26
288.15	0.2920	1491.74
288.15	0.3986	1499.22
288.15	0.4988	1508.48
288.15	0.5999	1516.07
288.15	0.6947	1523.59
288.15	0.7929	1531.19
298.15	0.0965	1503.48
298.15	0.2002	1511.04
298.15	0.2920	1517.62
298.15	0.3986	1525.38
298.15	0.4988	1532.21
298.15	0.5999	1542.37
298.15	0.6947	1551.24
298.15	0.7929	1560.56
308.15	0.0965	1525.09
308.15	0.2002	1531.28
308.15	0.2920	1536.87
308.15	0.3986	1543.31
308.15	0.4988	1550.94
308.15	0.5999	1563.23
308.15	0.6947	1572.72
308.15	0.7929	1582.65
318.15	0.0965	1543.95
318.15	0.2002	1552.21
318.15	0.2920	1560.57
318.15	0.3986	1567.78
318.15	0.4988	1576.89
318.15	0.5999	1584.48
318.15	0.6947	1592.31
318.15	0.7929	1600.48

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Molality, mol/kg of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0965	293.15	1489.87
0.2002	293.15	1498.03
0.2920	293.15	1504.81
0.3986	293.15	1513.14
0.4988	293.15	1520.51
0.0965	298.15	1503.48
0.2002	298.15	1511.04
0.2920	298.15	1517.62
0.3986	298.15	1525.38
0.4988	298.15	1532.21
0.0965	303.15	1514.85
0.2002	303.15	1521.76
0.2920	303.15	1528.02
0.3986	303.15	1535.06
0.4988	303.15	1541.68
0.0965	308.15	1525.09
0.2002	308.15	1531.28
0.2920	308.15	1536.87
0.3986	308.15	1543.31
0.4988	308.15	1549.44

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	0.9840	373.62
100.00	0.9690	373.90
100.00	0.9650	374.47
100.00	0.9400	375.25
100.00	0.9240	375.70
100.00	0.9210	375.88
100.00	0.8710	377.91
100.00	0.8490	378.31
100.00	0.8260	379.18
100.00	0.7770	381.73
100.00	0.7460	383.25
100.00	0.6920	386.87
100.00	0.6210	390.44
100.00	0.6000	392.66
100.00	0.5500	396.85
100.00	0.4910	401.01
100.00	0.4050	411.58
100.00	0.3540	420.64
70.00	0.9870	364.38
70.00	0.9740	363.83
70.00	0.9580	364.67
70.00	0.9370	365.45
70.00	0.9180	366.07
70.00	0.8970	366.65
70.00	0.8650	367.95
70.00	0.8230	369.20
70.00	0.8040	369.85
70.00	0.7530	371.85
70.00	0.7100	374.65
70.00	0.6560	377.39
70.00	0.6010	381.32
70.00	0.5330	385.24
70.00	0.4550	393.15
70.00	0.3390	410.80
50.00	0.9740	355.04
50.00	0.9600	355.65
50.00	0.9390	356.13
50.00	0.9270	356.56
50.00	0.9150	356.91
50.00	0.8700	358.86
50.00	0.8010	360.77
50.00	0.7800	361.79
50.00	0.7520	363.25
50.00	0.7160	364.79
50.00	0.7060	365.69
50.00	0.6440	368.60
50.00	0.5430	374.33
50.00	0.4920	378.79
50.00	0.4350	387.20
50.00	0.4300	388.70
50.00	0.3670	395.52

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1170	421.25
0.1400	417.15
0.1610	416.25
0.1760	414.75
0.1820	413.65
0.2420	413.25
0.2510	412.55
0.3250	403.95
0.3730	400.85
0.4100	397.95
0.5430	390.45
0.7040	380.15
0.7810	376.65
0.8260	374.95
0.8560	373.95
0.8770	372.95
0.8930	372.35
0.9150	371.55

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	0.9840	373.62
100.00	0.9690	373.90
100.00	0.9650	374.47
100.00	0.9400	375.25
100.00	0.9240	375.70
100.00	0.9210	375.88
100.00	0.8710	377.91
100.00	0.8490	378.31
100.00	0.8260	379.18
100.00	0.7770	381.73
100.00	0.7460	383.25
100.00	0.6920	386.87
100.00	0.6210	390.44
100.00	0.6000	392.66
100.00	0.5500	396.85
100.00	0.4910	401.01
100.00	0.4050	411.58
100.00	0.3540	420.64
70.00	0.9870	364.38
70.00	0.9740	363.83
70.00	0.9580	364.67
70.00	0.9370	365.45
70.00	0.9180	366.07
70.00	0.8970	366.65
70.00	0.8650	367.95
70.00	0.8230	369.20
70.00	0.8040	369.85
70.00	0.7530	371.85
70.00	0.7100	374.65
70.00	0.6560	377.39
70.00	0.6010	381.32
70.00	0.5330	385.24
70.00	0.4550	393.15
70.00	0.3390	410.80
50.00	0.9740	355.04
50.00	0.9600	355.65
50.00	0.9390	356.13
50.00	0.9270	356.56
50.00	0.9150	356.91
50.00	0.8700	358.86
50.00	0.8010	360.77
50.00	0.7800	361.79
50.00	0.7520	363.25
50.00	0.7160	364.79
50.00	0.7060	365.69
50.00	0.6440	368.60
50.00	0.5430	374.33
50.00	0.4920	378.79
50.00	0.4350	387.20
50.00	0.4300	388.70
50.00	0.3670	395.52

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 85 (Liquid)

Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1170	421.25
0.1400	417.15
0.1610	416.25
0.1760	414.75
0.1820	413.65
0.2420	413.25
0.2510	412.55
0.3250	403.95
0.3730	400.85
0.4100	397.95
0.5430	390.45
0.7040	380.15
0.7810	376.65
0.8260	374.95
0.8560	373.95
0.8770	372.95
0.8930	372.35
0.9150	371.55

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
0.2500	295.00	0.2580
0.2500	323.80	0.2680
0.2500	349.10	0.2750
0.2500	373.80	0.2800
0.2500	396.40	0.2850
0.2500	421.30	0.2920
0.2500	445.00	0.2820
0.5000	295.50	0.2100
0.5000	324.60	0.2160
0.5000	349.50	0.2190
0.5000	373.60	0.2200
0.5000	396.00	0.2210
0.5000	421.90	0.2210
0.5000	448.30	0.2160
0.7500	295.50	0.1950
0.7500	327.10	0.1970
0.7500	349.80	0.2010
0.7500	372.70	0.2020
0.7500	397.60	0.2000
0.7500	422.50	0.1980
0.7500	446.50	0.1950

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Triethylene glycol (1) - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
0.2500	295.00	0.2580
0.2500	323.80	0.2680
0.2500	349.10	0.2750
0.2500	373.80	0.2800
0.2500	396.40	0.2850
0.2500	421.30	0.2920
0.2500	445.00	0.2820
0.5000	295.50	0.2100
0.5000	324.60	0.2160
0.5000	349.50	0.2190
0.5000	373.60	0.2200
0.5000	396.00	0.2210
0.5000	421.90	0.2210
0.5000	448.30	0.2160
0.7500	295.50	0.1950
0.7500	327.10	0.1970
0.7500	349.80	0.2010
0.7500	372.70	0.2020
0.7500	397.60	0.2000
0.7500	422.50	0.1980
0.7500	446.50	0.1950

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 Triethylene glycol (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

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 Triethylene glycol (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
• Temperature change from isenthalpic expansion of aqueous triethylene glycol mixtures for natural gas dehydration
• Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
• 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
• 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
• Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
• Vapor-Liquid Equilibria of Water + Triethylene Glycol (TEG) and Water + TEG + Toluene at 85 kPa
• Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K