Mixture of 1,2-Hexanediol + Water

Datasets

1. Excess molar heat capacity, J/K/mol (2)
2. ρ_l - Mass density, kg/m3 (2)
3. γ - Surface tension liquid-gas, N/m (2)
4. Excess molar volume, m3/mol (2)

Excess molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Hexanediol (1) - Liquid	Excess molar heat capacity, J/K/mol - Liquid
283.15	0.0499	-0.1600
283.15	0.0995	-2.47
283.15	0.1989	-2.23
283.15	0.4015	-2.3
283.15	0.4841	-1.96
283.15	0.5535	-0.7800
283.15	0.6972	-1.03
283.15	0.7927	-0.6000
283.15	0.8822	-1.35
283.15	0.9437	0.0400
283.15	0.9784	-1.61
293.15	0.0499	0.3500
293.15	0.0995	-0.2300
293.15	0.1989	0.6800
293.15	0.2988	1.31
293.15	0.4015	0.8900
293.15	0.4841	1.13
293.15	0.5535	1.45
293.15	0.6972	0.9000
293.15	0.7927	0.9200
293.15	0.8822	0.8200
293.15	0.9437	0.6800
298.15	0.0995	0.8700
298.15	0.1989	1.97
298.15	0.2988	2.52
298.15	0.4015	2.19
298.15	0.4841	2.22
298.15	0.5535	2.33
298.15	0.6972	1.63
298.15	0.7927	1.26
298.15	0.8822	0.9400
298.15	0.9437	0.4700
303.15	0.0499	1.74
303.15	0.0995	1.95
303.15	0.1989	3.16
303.15	0.2988	3.76
303.15	0.4015	3.35
303.15	0.4841	3.15
303.15	0.5535	3.16
303.15	0.6972	2.27
303.15	0.7927	1.52
303.15	0.8822	0.8900
303.15	0.9437	0.2200
313.15	0.0499	2.85
313.15	0.0995	3.92
313.15	0.1989	5.28
313.15	0.2988	5.95
313.15	0.4015	5.35
313.15	0.4841	4.97
313.15	0.6972	3.48
313.15	0.7927	2.27
313.15	0.8822	1.65
313.15	0.9437	0.6200

Excess molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Hexanediol (1) - Liquid	Excess molar heat capacity, J/K/mol - Liquid
283.15	0.0499	-0.1600
283.15	0.0995	-2.47
283.15	0.1989	-2.23
283.15	0.4015	-2.3
283.15	0.4841	-1.96
283.15	0.5535	-0.7800
283.15	0.6972	-1.03
283.15	0.7927	-0.6000
283.15	0.8822	-1.35
283.15	0.9437	0.0400
283.15	0.9784	-1.61
293.15	0.0499	0.3500
293.15	0.0995	-0.2300
293.15	0.1989	0.6800
293.15	0.2988	1.31
293.15	0.4015	0.8900
293.15	0.4841	1.13
293.15	0.5535	1.45
293.15	0.6972	0.9000
293.15	0.7927	0.9200
293.15	0.8822	0.8200
293.15	0.9437	0.6800
298.15	0.0995	0.8700
298.15	0.1989	1.97
298.15	0.2988	2.52
298.15	0.4015	2.19
298.15	0.4841	2.22
298.15	0.5535	2.33
298.15	0.6972	1.63
298.15	0.7927	1.26
298.15	0.8822	0.9400
298.15	0.9437	0.4700
303.15	0.0499	1.74
303.15	0.0995	1.95
303.15	0.1989	3.16
303.15	0.2988	3.76
303.15	0.4015	3.35
303.15	0.4841	3.15
303.15	0.5535	3.16
303.15	0.6972	2.27
303.15	0.7927	1.52
303.15	0.8822	0.8900
303.15	0.9437	0.2200
313.15	0.0499	2.85
313.15	0.0995	3.92
313.15	0.1989	5.28
313.15	0.2988	5.95
313.15	0.4015	5.35
313.15	0.4841	4.97
313.15	0.6972	3.48
313.15	0.7927	2.27
313.15	0.8822	1.65
313.15	0.9437	0.6200

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Hexanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	283.15	999.69
0.0009	283.15	999.77
0.0018	283.15	999.85
0.0036	283.15	1000.05
0.0055	283.15	1000.31
0.0077	283.15	1000.69
0.0090	283.15	1000.93
0.0106	283.15	1001.22
0.0124	283.15	1001.49
0.0143	283.15	1001.65
0.0160	283.15	1001.69
0.0178	283.15	1001.64
0.0351	283.15	999.52
0.0672	283.15	995.27
0.0968	283.15	991.84
0.1119	283.15	990.47
0.0000	288.15	999.1
0.0009	288.15	999.33
0.0018	288.15	999.35
0.0036	288.15	999.43
0.0055	288.15	999.57
0.0077	288.15	999.81
0.0090	288.15	999.97
0.0106	288.15	1000.16
0.0124	288.15	1000.33
0.0143	288.15	1000.41
0.0160	288.15	1000.38
0.0178	288.15	1000.25
0.0351	288.15	997.75
0.0672	288.15	993.06
0.0968	288.15	989.37
0.1119	288.15	987.91
0.0000	293.15	998.21
0.0009	293.15	998.26
0.0018	293.15	998.28
0.0036	293.15	998.39
0.0055	293.15	998.54
0.0077	293.15	998.75
0.0090	293.15	998.86
0.0106	293.15	998.97
0.0124	293.15	999.03
0.0143	293.15	999.01
0.0160	293.15	998.91
0.0178	293.15	998.73
0.0351	293.15	995.76
0.0672	293.15	990.72
0.0968	293.15	986.7
0.1119	293.15	985.24
0.0000	298.15	997.04
0.0009	298.15	997.06
0.0018	298.15	997.06
0.0036	298.15	997.13
0.0055	298.15	997.24
0.0077	298.15	997.43
0.0090	298.15	997.49
0.0106	298.15	997.52
0.0124	298.15	997.47
0.0143	298.15	997.32
0.0160	298.15	997.13
0.0178	298.15	996.87
0.0351	298.15	993.77
0.0672	298.15	988.37
0.0968	298.15	983.93
0.1119	298.15	982.11
0.0000	303.15	995.65
0.0009	303.15	995.65
0.0018	303.15	995.66
0.0036	303.15	995.76
0.0055	303.15	995.78
0.0077	303.15	995.64
0.0090	303.15	995.53
0.0106	303.15	995.37
0.0124	303.15	995.17
0.0143	303.15	994.93
0.0160	303.15	994.7
0.0178	303.15	994.45
0.0351	303.15	991.54
0.0672	303.15	985.8
0.0968	303.15	981.37
0.1119	303.15	979.56
0.0000	308.15	994.03
0.0009	308.15	993.92
0.0018	308.15	993.92
0.0036	308.15	993.98
0.0055	308.15	994.13
0.0077	308.15	994.2274
0.0090	308.15	994.2776
0.0106	308.15	994.2763
0.0124	308.15	994.1413
0.0143	308.15	993.8174
0.0160	308.15	993.3949
0.0178	308.15	992.8687
0.0351	308.15	988.24
0.0672	308.15	981.8469
0.0968	308.15	977.5691
0.1119	308.15	975.7462

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Hexanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	283.15	999.69
0.0009	283.15	999.77
0.0018	283.15	999.85
0.0036	283.15	1000.05
0.0055	283.15	1000.31
0.0077	283.15	1000.69
0.0090	283.15	1000.93
0.0106	283.15	1001.22
0.0124	283.15	1001.49
0.0143	283.15	1001.65
0.0160	283.15	1001.69
0.0178	283.15	1001.64
0.0351	283.15	999.52
0.0672	283.15	995.27
0.0968	283.15	991.84
0.1119	283.15	990.47
0.0000	288.15	999.1
0.0009	288.15	999.33
0.0018	288.15	999.35
0.0036	288.15	999.43
0.0055	288.15	999.57
0.0077	288.15	999.81
0.0090	288.15	999.97
0.0106	288.15	1000.16
0.0124	288.15	1000.33
0.0143	288.15	1000.41
0.0160	288.15	1000.38
0.0178	288.15	1000.25
0.0351	288.15	997.75
0.0672	288.15	993.06
0.0968	288.15	989.37
0.1119	288.15	987.91
0.0000	293.15	998.21
0.0009	293.15	998.26
0.0018	293.15	998.28
0.0036	293.15	998.39
0.0055	293.15	998.54
0.0077	293.15	998.75
0.0090	293.15	998.86
0.0106	293.15	998.97
0.0124	293.15	999.03
0.0143	293.15	999.01
0.0160	293.15	998.91
0.0178	293.15	998.73
0.0351	293.15	995.76
0.0672	293.15	990.72
0.0968	293.15	986.7
0.1119	293.15	985.24
0.0000	298.15	997.04
0.0009	298.15	997.06
0.0018	298.15	997.06
0.0036	298.15	997.13
0.0055	298.15	997.24
0.0077	298.15	997.43
0.0090	298.15	997.49
0.0106	298.15	997.52
0.0124	298.15	997.47
0.0143	298.15	997.32
0.0160	298.15	997.13
0.0178	298.15	996.87
0.0351	298.15	993.77
0.0672	298.15	988.37
0.0968	298.15	983.93
0.1119	298.15	982.11
0.0000	303.15	995.65
0.0009	303.15	995.65
0.0018	303.15	995.66
0.0036	303.15	995.76
0.0055	303.15	995.78
0.0077	303.15	995.64
0.0090	303.15	995.53
0.0106	303.15	995.37
0.0124	303.15	995.17
0.0143	303.15	994.93
0.0160	303.15	994.7
0.0178	303.15	994.45
0.0351	303.15	991.54
0.0672	303.15	985.8
0.0968	303.15	981.37
0.1119	303.15	979.56
0.0000	308.15	994.03
0.0009	308.15	993.92
0.0018	308.15	993.92
0.0036	308.15	993.98
0.0055	308.15	994.13
0.0077	308.15	994.2274
0.0090	308.15	994.2776
0.0106	308.15	994.2763
0.0124	308.15	994.1413
0.0143	308.15	993.8174
0.0160	308.15	993.3949
0.0178	308.15	992.8687
0.0351	308.15	988.24
0.0672	308.15	981.8469
0.0968	308.15	977.5691
0.1119	308.15	975.7462

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Hexanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0000	0.0741
283.15	0.0010	0.0551
283.15	0.0016	0.0475
283.15	0.0020	0.0451
283.15	0.0034	0.0416
283.15	0.0052	0.0373
283.15	0.0077	0.0322
283.15	0.0108	0.0287
283.15	0.0140	0.0276
283.15	0.0175	0.0264
283.15	0.0251	0.0262
283.15	0.0360	0.0257
283.15	0.0460	0.0257
283.15	0.0514	0.0257
283.15	0.0655	0.0256
283.15	0.0831	0.0256
283.15	0.0968	0.0251
283.15	0.1119	0.0249
283.15	1.0000	0.0247
288.15	0.0000	0.0734
288.15	0.0010	0.0545
288.15	0.0016	0.0473
288.15	0.0020	0.0445
288.15	0.0034	0.0406
288.15	0.0052	0.0363
288.15	0.0077	0.0314
288.15	0.0108	0.0281
288.15	0.0140	0.0269
288.15	0.0175	0.0259
288.15	0.0251	0.0259
288.15	0.0360	0.0255
288.15	0.0460	0.0254
288.15	0.0514	0.0254
288.15	0.0655	0.0254
288.15	0.0831	0.0253
288.15	0.0968	0.0249
288.15	0.1119	0.0247
288.15	1.0000	0.0244
293.15	0.0000	0.0726
293.15	0.0010	0.0543
293.15	0.0016	0.0470
293.15	0.0020	0.0439
293.15	0.0034	0.0400
293.15	0.0052	0.0355
293.15	0.0077	0.0308
293.15	0.0108	0.0277
293.15	0.0140	0.0263
293.15	0.0175	0.0257
293.15	0.0251	0.0255
293.15	0.0360	0.0252
293.15	0.0460	0.0252
293.15	0.0514	0.0252
293.15	0.0655	0.0251
293.15	0.0831	0.0251
293.15	0.0968	0.0246
293.15	0.1119	0.0244
293.15	1.0000	0.0241
298.15	0.0000	0.0718
298.15	0.0010	0.0538
298.15	0.0016	0.0466
298.15	0.0020	0.0434
298.15	0.0034	0.0393
298.15	0.0052	0.0347
298.15	0.0077	0.0300
298.15	0.0108	0.0272
298.15	0.0140	0.0257
298.15	0.0175	0.0253
298.15	0.0251	0.0252
298.15	0.0360	0.0250
298.15	0.0460	0.0249
298.15	0.0514	0.0249
298.15	0.0655	0.0249
298.15	0.0831	0.0248
298.15	0.0968	0.0244
298.15	0.1119	0.0241
298.15	1.0000	0.0238
303.15	0.0000	0.0710
303.15	0.0010	0.0533
303.15	0.0016	0.0463
303.15	0.0020	0.0428
303.15	0.0034	0.0385
303.15	0.0052	0.0338
303.15	0.0077	0.0295
303.15	0.0108	0.0268
303.15	0.0140	0.0252
303.15	0.0175	0.0248
303.15	0.0251	0.0250
303.15	0.0360	0.0247
303.15	0.0460	0.0247
303.15	0.0514	0.0247
303.15	0.0655	0.0244
303.15	0.0831	0.0245
303.15	0.0968	0.0243
303.15	0.1119	0.0239
303.15	1.0000	0.0236
308.15	0.0000	0.0702
308.15	0.0010	0.0527
308.15	0.0016	0.0456
308.15	0.0020	0.0423
308.15	0.0034	0.0381
308.15	0.0052	0.0330
308.15	0.0077	0.0289
308.15	0.0108	0.0264
308.15	0.0140	0.0248
308.15	0.0175	0.0244
308.15	0.0251	0.0247
308.15	0.0360	0.0245
308.15	0.0460	0.0244
308.15	0.0514	0.0244
308.15	0.0655	0.0241
308.15	0.0831	0.0241
308.15	0.0968	0.0240
308.15	0.1119	0.0236
308.15	1.0000	0.0233

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Hexanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0000	0.0741
283.15	0.0010	0.0551
283.15	0.0016	0.0475
283.15	0.0020	0.0451
283.15	0.0034	0.0416
283.15	0.0052	0.0373
283.15	0.0077	0.0322
283.15	0.0108	0.0287
283.15	0.0140	0.0276
283.15	0.0175	0.0264
283.15	0.0251	0.0262
283.15	0.0360	0.0257
283.15	0.0460	0.0257
283.15	0.0514	0.0257
283.15	0.0655	0.0256
283.15	0.0831	0.0256
283.15	0.0968	0.0251
283.15	0.1119	0.0249
283.15	1.0000	0.0247
288.15	0.0000	0.0734
288.15	0.0010	0.0545
288.15	0.0016	0.0473
288.15	0.0020	0.0445
288.15	0.0034	0.0406
288.15	0.0052	0.0363
288.15	0.0077	0.0314
288.15	0.0108	0.0281
288.15	0.0140	0.0269
288.15	0.0175	0.0259
288.15	0.0251	0.0259
288.15	0.0360	0.0255
288.15	0.0460	0.0254
288.15	0.0514	0.0254
288.15	0.0655	0.0254
288.15	0.0831	0.0253
288.15	0.0968	0.0249
288.15	0.1119	0.0247
288.15	1.0000	0.0244
293.15	0.0000	0.0726
293.15	0.0010	0.0543
293.15	0.0016	0.0470
293.15	0.0020	0.0439
293.15	0.0034	0.0400
293.15	0.0052	0.0355
293.15	0.0077	0.0308
293.15	0.0108	0.0277
293.15	0.0140	0.0263
293.15	0.0175	0.0257
293.15	0.0251	0.0255
293.15	0.0360	0.0252
293.15	0.0460	0.0252
293.15	0.0514	0.0252
293.15	0.0655	0.0251
293.15	0.0831	0.0251
293.15	0.0968	0.0246
293.15	0.1119	0.0244
293.15	1.0000	0.0241
298.15	0.0000	0.0718
298.15	0.0010	0.0538
298.15	0.0016	0.0466
298.15	0.0020	0.0434
298.15	0.0034	0.0393
298.15	0.0052	0.0347
298.15	0.0077	0.0300
298.15	0.0108	0.0272
298.15	0.0140	0.0257
298.15	0.0175	0.0253
298.15	0.0251	0.0252
298.15	0.0360	0.0250
298.15	0.0460	0.0249
298.15	0.0514	0.0249
298.15	0.0655	0.0249
298.15	0.0831	0.0248
298.15	0.0968	0.0244
298.15	0.1119	0.0241
298.15	1.0000	0.0238
303.15	0.0000	0.0710
303.15	0.0010	0.0533
303.15	0.0016	0.0463
303.15	0.0020	0.0428
303.15	0.0034	0.0385
303.15	0.0052	0.0338
303.15	0.0077	0.0295
303.15	0.0108	0.0268
303.15	0.0140	0.0252
303.15	0.0175	0.0248
303.15	0.0251	0.0250
303.15	0.0360	0.0247
303.15	0.0460	0.0247
303.15	0.0514	0.0247
303.15	0.0655	0.0244
303.15	0.0831	0.0245
303.15	0.0968	0.0243
303.15	0.1119	0.0239
303.15	1.0000	0.0236
308.15	0.0000	0.0702
308.15	0.0010	0.0527
308.15	0.0016	0.0456
308.15	0.0020	0.0423
308.15	0.0034	0.0381
308.15	0.0052	0.0330
308.15	0.0077	0.0289
308.15	0.0108	0.0264
308.15	0.0140	0.0248
308.15	0.0175	0.0244
308.15	0.0251	0.0247
308.15	0.0360	0.0245
308.15	0.0460	0.0244
308.15	0.0514	0.0244
308.15	0.0655	0.0241
308.15	0.0831	0.0241
308.15	0.0968	0.0240
308.15	0.1119	0.0236
308.15	1.0000	0.0233

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Hexanediol (1) - Liquid	Excess molar volume, m3/mol - Liquid
283.15	0.0491	-2.0020e-07
283.15	0.0995	-2.8370e-07
283.15	0.1989	-3.9220e-07
283.15	0.2988	-4.4330e-07
283.15	0.4015	-4.5050e-07
283.15	0.4841	-4.3100e-07
283.15	0.5535	-3.9770e-07
283.15	0.6972	-3.0340e-07
283.15	0.7927	-2.2190e-07
283.15	0.8822	-1.3470e-07
283.15	0.9437	-6.9200e-08
283.15	0.9784	-3.2200e-08
293.15	0.0491	-1.7480e-07
293.15	0.0995	-2.5060e-07
293.15	0.1989	-3.4950e-07
293.15	0.2988	-3.9620e-07
293.15	0.4015	-4.0320e-07
293.15	0.4841	-3.8560e-07
293.15	0.5535	-3.5630e-07
293.15	0.6972	-2.7070e-07
293.15	0.7927	-1.9800e-07
293.15	0.8822	-1.1990e-07
293.15	0.9437	-6.1800e-08
293.15	0.9784	-2.9400e-08
298.15	0.0491	-1.6460e-07
298.15	0.0995	-2.3690e-07
298.15	0.1989	-3.3150e-07
298.15	0.2988	-3.7620e-07
298.15	0.4015	-3.8310e-07
298.15	0.4841	-3.6660e-07
298.15	0.5535	-3.3920e-07
298.15	0.6972	-2.5750e-07
298.15	0.7927	-1.8820e-07
298.15	0.8822	-1.1380e-07
298.15	0.9437	-5.9000e-08
298.15	0.9784	-2.8100e-08
303.15	0.0491	-1.5570e-07
303.15	0.0995	-2.2470e-07
303.15	0.1989	-3.1490e-07
303.15	0.2988	-3.5780e-07
303.15	0.4015	-3.6440e-07
303.15	0.4841	-3.4870e-07
303.15	0.5535	-3.2330e-07
303.15	0.6972	-2.4500e-07
303.15	0.7927	-1.7970e-07
303.15	0.8822	-1.0910e-07
303.15	0.9437	-5.6900e-08
303.15	0.9784	-2.7200e-08
313.15	0.0491	-1.4050e-07
313.15	0.0995	-2.0330e-07
313.15	0.1989	-2.8510e-07
313.15	0.2988	-3.2390e-07
313.15	0.4015	-3.2970e-07
313.15	0.4841	-3.1570e-07
313.15	0.5535	-2.9340e-07
313.15	0.6972	-2.2230e-07
313.15	0.7927	-1.6330e-07
313.15	0.8822	-9.9200e-08
313.15	0.9437	-5.1900e-08
313.15	0.9784	-2.5700e-08

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Hexanediol (1) - Liquid	Excess molar volume, m3/mol - Liquid
283.15	0.0491	-2.0020e-07
283.15	0.0995	-2.8370e-07
283.15	0.1989	-3.9220e-07
283.15	0.2988	-4.4330e-07
283.15	0.4015	-4.5050e-07
283.15	0.4841	-4.3100e-07
283.15	0.5535	-3.9770e-07
283.15	0.6972	-3.0340e-07
283.15	0.7927	-2.2190e-07
283.15	0.8822	-1.3470e-07
283.15	0.9437	-6.9200e-08
283.15	0.9784	-3.2200e-08
293.15	0.0491	-1.7480e-07
293.15	0.0995	-2.5060e-07
293.15	0.1989	-3.4950e-07
293.15	0.2988	-3.9620e-07
293.15	0.4015	-4.0320e-07
293.15	0.4841	-3.8560e-07
293.15	0.5535	-3.5630e-07
293.15	0.6972	-2.7070e-07
293.15	0.7927	-1.9800e-07
293.15	0.8822	-1.1990e-07
293.15	0.9437	-6.1800e-08
293.15	0.9784	-2.9400e-08
298.15	0.0491	-1.6460e-07
298.15	0.0995	-2.3690e-07
298.15	0.1989	-3.3150e-07
298.15	0.2988	-3.7620e-07
298.15	0.4015	-3.8310e-07
298.15	0.4841	-3.6660e-07
298.15	0.5535	-3.3920e-07
298.15	0.6972	-2.5750e-07
298.15	0.7927	-1.8820e-07
298.15	0.8822	-1.1380e-07
298.15	0.9437	-5.9000e-08
298.15	0.9784	-2.8100e-08
303.15	0.0491	-1.5570e-07
303.15	0.0995	-2.2470e-07
303.15	0.1989	-3.1490e-07
303.15	0.2988	-3.5780e-07
303.15	0.4015	-3.6440e-07
303.15	0.4841	-3.4870e-07
303.15	0.5535	-3.2330e-07
303.15	0.6972	-2.4500e-07
303.15	0.7927	-1.7970e-07
303.15	0.8822	-1.0910e-07
303.15	0.9437	-5.6900e-08
303.15	0.9784	-2.7200e-08
313.15	0.0491	-1.4050e-07
313.15	0.0995	-2.0330e-07
313.15	0.1989	-2.8510e-07
313.15	0.2988	-3.2390e-07
313.15	0.4015	-3.2970e-07
313.15	0.4841	-3.1570e-07
313.15	0.5535	-2.9340e-07
313.15	0.6972	-2.2230e-07
313.15	0.7927	-1.6330e-07
313.15	0.8822	-9.9200e-08
313.15	0.9437	-5.1900e-08
313.15	0.9784	-2.5700e-08

Sources

• Effect of temperature on the surface tension of diluted aqueous solutions of 1,2-hexanediol, 1,5-hexanediol, 1,6-hexanediol and 2,5-hexanediol
• Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
• Effect of temperature on the volumetric properties of dilute aqueous solutions of 1,2-hexanediol, 1,5-hexanediol, 1,6-hexanediol, and 2,5-hexanediol