Mixture of Tetraglyme + 1-Butanol

Datasets

1. η - Viscosity, Pa*s (2)
2. n₀ - Refractive index (Na D-line) (2)
3. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0043
288.15	0.1013	0.0041
288.15	0.2236	0.0038
288.15	0.3036	0.0036
288.15	0.4131	0.0033
288.15	0.5065	0.0031
288.15	0.5996	0.0029
288.15	0.7007	0.0028
288.15	0.7991	0.0027
288.15	0.8996	0.0029
288.15	1.0000	0.0034
293.15	0.0000	0.0038
293.15	0.1013	0.0036
293.15	0.2236	0.0033
293.15	0.3036	0.0031
293.15	0.4131	0.0029
293.15	0.5065	0.0028
293.15	0.5996	0.0026
293.15	0.7007	0.0025
293.15	0.7991	0.0024
293.15	0.8996	0.0025
293.15	1.0000	0.0030
298.15	0.0000	0.0034
298.15	0.1013	0.0032
298.15	0.2236	0.0029
298.15	0.3036	0.0028
298.15	0.4131	0.0026
298.15	0.5065	0.0025
298.15	0.5996	0.0023
298.15	0.7007	0.0022
298.15	0.7991	0.0022
298.15	0.8996	0.0023
298.15	1.0000	0.0026
303.15	0.0000	0.0030
303.15	0.1013	0.0028
303.15	0.2236	0.0026
303.15	0.3036	0.0025
303.15	0.4131	0.0023
303.15	0.5065	0.0022
303.15	0.5996	0.0021
303.15	0.7007	0.0020
303.15	0.7991	0.0019
303.15	0.8996	0.0020
303.15	1.0000	0.0023
308.15	0.0000	0.0027
308.15	0.1013	0.0025
308.15	0.2236	0.0024
308.15	0.3036	0.0022
308.15	0.4131	0.0021
308.15	0.5065	0.0020
308.15	0.5996	0.0019
308.15	0.7007	0.0018
308.15	0.7991	0.0018
308.15	0.8996	0.0018
308.15	1.0000	0.0020
313.15	0.0000	0.0024
313.15	0.1013	0.0023
313.15	0.2236	0.0021
313.15	0.3036	0.0020
313.15	0.4131	0.0019
313.15	0.5065	0.0018
313.15	0.5996	0.0017
313.15	0.7007	0.0016
313.15	0.7991	0.0016
313.15	0.8996	0.0016
313.15	1.0000	0.0018
318.15	0.0000	0.0022
318.15	0.1013	0.0021
318.15	0.2236	0.0019
318.15	0.3036	0.0019
318.15	0.4131	0.0017
318.15	0.5065	0.0017
318.15	0.5996	0.0016
318.15	0.7007	0.0015
318.15	0.7991	0.0014
318.15	0.8996	0.0015
318.15	1.0000	0.0016
323.15	0.0000	0.0020
323.15	0.1013	0.0019
323.15	0.2236	0.0018
323.15	0.3036	0.0017
323.15	0.4131	0.0016
323.15	0.5065	0.0015
323.15	0.5996	0.0014
323.15	0.7007	0.0014
323.15	0.7991	0.0013
323.15	0.8996	0.0013
323.15	1.0000	0.0014
328.15	0.0000	0.0018
328.15	0.1013	0.0017
328.15	0.2236	0.0016
328.15	0.3036	0.0016
328.15	0.4131	0.0015
328.15	0.5065	0.0014
328.15	0.5996	0.0013
328.15	0.7007	0.0013
328.15	0.7991	0.0012
328.15	0.8996	0.0012
328.15	1.0000	0.0013
333.15	0.0000	0.0017
333.15	0.1013	0.0016
333.15	0.2236	0.0015
333.15	0.3036	0.0014
333.15	0.4131	0.0014
333.15	0.5065	0.0013
333.15	0.5996	0.0012
333.15	0.7007	0.0012
333.15	0.7991	0.0011
333.15	0.8996	0.0011
333.15	1.0000	0.0011

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Viscosity, Pa*s - Liquid
288.15	0.0000	0.0043
288.15	0.1013	0.0041
288.15	0.2236	0.0038
288.15	0.3036	0.0036
288.15	0.4131	0.0033
288.15	0.5065	0.0031
288.15	0.5996	0.0029
288.15	0.7007	0.0028
288.15	0.7991	0.0027
288.15	0.8996	0.0029
288.15	1.0000	0.0034
293.15	0.0000	0.0038
293.15	0.1013	0.0036
293.15	0.2236	0.0033
293.15	0.3036	0.0031
293.15	0.4131	0.0029
293.15	0.5065	0.0028
293.15	0.5996	0.0026
293.15	0.7007	0.0025
293.15	0.7991	0.0024
293.15	0.8996	0.0025
293.15	1.0000	0.0030
298.15	0.0000	0.0034
298.15	0.1013	0.0032
298.15	0.2236	0.0029
298.15	0.3036	0.0028
298.15	0.4131	0.0026
298.15	0.5065	0.0025
298.15	0.5996	0.0023
298.15	0.7007	0.0022
298.15	0.7991	0.0022
298.15	0.8996	0.0023
298.15	1.0000	0.0026
303.15	0.0000	0.0030
303.15	0.1013	0.0028
303.15	0.2236	0.0026
303.15	0.3036	0.0025
303.15	0.4131	0.0023
303.15	0.5065	0.0022
303.15	0.5996	0.0021
303.15	0.7007	0.0020
303.15	0.7991	0.0019
303.15	0.8996	0.0020
303.15	1.0000	0.0023
308.15	0.0000	0.0027
308.15	0.1013	0.0025
308.15	0.2236	0.0024
308.15	0.3036	0.0022
308.15	0.4131	0.0021
308.15	0.5065	0.0020
308.15	0.5996	0.0019
308.15	0.7007	0.0018
308.15	0.7991	0.0018
308.15	0.8996	0.0018
308.15	1.0000	0.0020
313.15	0.0000	0.0024
313.15	0.1013	0.0023
313.15	0.2236	0.0021
313.15	0.3036	0.0020
313.15	0.4131	0.0019
313.15	0.5065	0.0018
313.15	0.5996	0.0017
313.15	0.7007	0.0016
313.15	0.7991	0.0016
313.15	0.8996	0.0016
313.15	1.0000	0.0018
318.15	0.0000	0.0022
318.15	0.1013	0.0021
318.15	0.2236	0.0019
318.15	0.3036	0.0019
318.15	0.4131	0.0017
318.15	0.5065	0.0017
318.15	0.5996	0.0016
318.15	0.7007	0.0015
318.15	0.7991	0.0014
318.15	0.8996	0.0015
318.15	1.0000	0.0016
323.15	0.0000	0.0020
323.15	0.1013	0.0019
323.15	0.2236	0.0018
323.15	0.3036	0.0017
323.15	0.4131	0.0016
323.15	0.5065	0.0015
323.15	0.5996	0.0014
323.15	0.7007	0.0014
323.15	0.7991	0.0013
323.15	0.8996	0.0013
323.15	1.0000	0.0014
328.15	0.0000	0.0018
328.15	0.1013	0.0017
328.15	0.2236	0.0016
328.15	0.3036	0.0016
328.15	0.4131	0.0015
328.15	0.5065	0.0014
328.15	0.5996	0.0013
328.15	0.7007	0.0013
328.15	0.7991	0.0012
328.15	0.8996	0.0012
328.15	1.0000	0.0013
333.15	0.0000	0.0017
333.15	0.1013	0.0016
333.15	0.2236	0.0015
333.15	0.3036	0.0014
333.15	0.4131	0.0014
333.15	0.5065	0.0013
333.15	0.5996	0.0012
333.15	0.7007	0.0012
333.15	0.7991	0.0011
333.15	0.8996	0.0011
333.15	1.0000	0.0011

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4345
288.15	0.1013	1.4329
288.15	0.2236	1.4308
288.15	0.3036	1.4294
288.15	0.4131	1.4269
288.15	0.5065	1.4246
288.15	0.5996	1.4219
288.15	0.7007	1.4182
288.15	0.7991	1.4138
288.15	0.8996	1.4082
288.15	1.0000	1.4013
293.15	0.0000	1.4324
293.15	0.1013	1.4308
293.15	0.2236	1.4287
293.15	0.3036	1.4273
293.15	0.4131	1.4248
293.15	0.5065	1.4226
293.15	0.5996	1.4198
293.15	0.7007	1.4161
293.15	0.7991	1.4118
293.15	0.8996	1.4062
293.15	1.0000	1.3993
298.15	0.0000	1.4303
298.15	0.1013	1.4287
298.15	0.2236	1.4266
298.15	0.3036	1.4252
298.15	0.4131	1.4227
298.15	0.5065	1.4204
298.15	0.5996	1.4177
298.15	0.7007	1.4141
298.15	0.7991	1.4097
298.15	0.8996	1.4042
298.15	1.0000	1.3973
303.15	0.0000	1.4282
303.15	0.1013	1.4266
303.15	0.2236	1.4245
303.15	0.3036	1.4231
303.15	0.4131	1.4206
303.15	0.5065	1.4183
303.15	0.5996	1.4156
303.15	0.7007	1.412
303.15	0.7991	1.4077
303.15	0.8996	1.4022
303.15	1.0000	1.3953
308.15	0.0000	1.426
308.15	0.1013	1.4245
308.15	0.2236	1.4224
308.15	0.3036	1.4209
308.15	0.4131	1.4185
308.15	0.5065	1.4162
308.15	0.5996	1.4135
308.15	0.7007	1.4099
308.15	0.7991	1.4056
308.15	0.8996	1.4001
308.15	1.0000	1.3932
313.15	0.0000	1.4239
313.15	0.1013	1.4224
313.15	0.2236	1.4202
313.15	0.3036	1.4188
313.15	0.4131	1.4163
313.15	0.5065	1.414
313.15	0.5996	1.4113
313.15	0.7007	1.4078
313.15	0.7991	1.4035
313.15	0.8996	1.398
313.15	1.0000	1.391
318.15	0.0000	1.4218
318.15	0.1013	1.4203
318.15	0.2236	1.4182
318.15	0.3036	1.4167
318.15	0.4131	1.4142
318.15	0.5065	1.4119
318.15	0.5996	1.4092
318.15	0.7007	1.4056
318.15	0.7991	1.4013
318.15	0.8996	1.3958
318.15	1.0000	1.3889
323.15	0.0000	1.4197
323.15	0.1013	1.4182
323.15	0.2236	1.416
323.15	0.3036	1.4146
323.15	0.4131	1.4121
323.15	0.5065	1.4098
323.15	0.5996	1.4071
323.15	0.7007	1.4035
323.15	0.7991	1.3992
323.15	0.8996	1.3937
323.15	1.0000	1.3868
328.15	0.0000	1.4177
328.15	0.1013	1.4161
328.15	0.2236	1.414
328.15	0.3036	1.4125
328.15	0.4131	1.41
328.15	0.5065	1.4076
328.15	0.5996	1.4049
328.15	0.7007	1.4013
328.15	0.7991	1.3971
328.15	0.8996	1.3916
328.15	1.0000	1.3847
333.15	0.0000	1.4155
333.15	0.1013	1.414
333.15	0.2236	1.4119
333.15	0.3036	1.4104
333.15	0.4131	1.4078
333.15	0.5065	1.4055
333.15	0.5996	1.4027
333.15	0.7007	1.3992
333.15	0.7991	1.395
333.15	0.8996	1.3894
333.15	1.0000	1.3824

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Refractive index (Na D-line) - Liquid
288.15	0.0000	1.4345
288.15	0.1013	1.4329
288.15	0.2236	1.4308
288.15	0.3036	1.4294
288.15	0.4131	1.4269
288.15	0.5065	1.4246
288.15	0.5996	1.4219
288.15	0.7007	1.4182
288.15	0.7991	1.4138
288.15	0.8996	1.4082
288.15	1.0000	1.4013
293.15	0.0000	1.4324
293.15	0.1013	1.4308
293.15	0.2236	1.4287
293.15	0.3036	1.4273
293.15	0.4131	1.4248
293.15	0.5065	1.4226
293.15	0.5996	1.4198
293.15	0.7007	1.4161
293.15	0.7991	1.4118
293.15	0.8996	1.4062
293.15	1.0000	1.3993
298.15	0.0000	1.4303
298.15	0.1013	1.4287
298.15	0.2236	1.4266
298.15	0.3036	1.4252
298.15	0.4131	1.4227
298.15	0.5065	1.4204
298.15	0.5996	1.4177
298.15	0.7007	1.4141
298.15	0.7991	1.4097
298.15	0.8996	1.4042
298.15	1.0000	1.3973
303.15	0.0000	1.4282
303.15	0.1013	1.4266
303.15	0.2236	1.4245
303.15	0.3036	1.4231
303.15	0.4131	1.4206
303.15	0.5065	1.4183
303.15	0.5996	1.4156
303.15	0.7007	1.412
303.15	0.7991	1.4077
303.15	0.8996	1.4022
303.15	1.0000	1.3953
308.15	0.0000	1.426
308.15	0.1013	1.4245
308.15	0.2236	1.4224
308.15	0.3036	1.4209
308.15	0.4131	1.4185
308.15	0.5065	1.4162
308.15	0.5996	1.4135
308.15	0.7007	1.4099
308.15	0.7991	1.4056
308.15	0.8996	1.4001
308.15	1.0000	1.3932
313.15	0.0000	1.4239
313.15	0.1013	1.4224
313.15	0.2236	1.4202
313.15	0.3036	1.4188
313.15	0.4131	1.4163
313.15	0.5065	1.414
313.15	0.5996	1.4113
313.15	0.7007	1.4078
313.15	0.7991	1.4035
313.15	0.8996	1.398
313.15	1.0000	1.391
318.15	0.0000	1.4218
318.15	0.1013	1.4203
318.15	0.2236	1.4182
318.15	0.3036	1.4167
318.15	0.4131	1.4142
318.15	0.5065	1.4119
318.15	0.5996	1.4092
318.15	0.7007	1.4056
318.15	0.7991	1.4013
318.15	0.8996	1.3958
318.15	1.0000	1.3889
323.15	0.0000	1.4197
323.15	0.1013	1.4182
323.15	0.2236	1.416
323.15	0.3036	1.4146
323.15	0.4131	1.4121
323.15	0.5065	1.4098
323.15	0.5996	1.4071
323.15	0.7007	1.4035
323.15	0.7991	1.3992
323.15	0.8996	1.3937
323.15	1.0000	1.3868
328.15	0.0000	1.4177
328.15	0.1013	1.4161
328.15	0.2236	1.414
328.15	0.3036	1.4125
328.15	0.4131	1.41
328.15	0.5065	1.4076
328.15	0.5996	1.4049
328.15	0.7007	1.4013
328.15	0.7991	1.3971
328.15	0.8996	1.3916
328.15	1.0000	1.3847
333.15	0.0000	1.4155
333.15	0.1013	1.414
333.15	0.2236	1.4119
333.15	0.3036	1.4104
333.15	0.4131	1.4078
333.15	0.5065	1.4055
333.15	0.5996	1.4027
333.15	0.7007	1.3992
333.15	0.7991	1.395
333.15	0.8996	1.3894
333.15	1.0000	1.3824

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1015.63
288.15	0.1013	1006.514
288.15	0.2236	993.986
288.15	0.3036	984.642
288.15	0.4131	969.983
288.15	0.5065	955.349
288.15	0.5996	938.288
288.15	0.7007	916.154
288.15	0.7991	889.873
288.15	0.8996	856.379
288.15	1.0000	813.407
293.15	0.0000	1010.995
293.15	0.1013	1001.909
293.15	0.2236	989.415
293.15	0.3036	980.1
293.15	0.4131	965.493
293.15	0.5065	950.916
293.15	0.5996	933.921
293.15	0.7007	911.881
293.15	0.7991	885.715
293.15	0.8996	852.384
293.15	1.0000	809.621
298.15	0.0000	1006.359
298.15	0.1013	997.307
298.15	0.2236	984.881
298.15	0.3036	975.56
298.15	0.4131	960.897
298.15	0.5065	946.305
298.15	0.5996	929.548
298.15	0.7007	907.599
298.15	0.7991	881.548
298.15	0.8996	848.369
298.15	1.0000	805.804
303.15	0.0000	1001.732
303.15	0.1013	992.702
303.15	0.2236	980.276
303.15	0.3036	971.014
303.15	0.4131	956.499
303.15	0.5065	942.026
303.15	0.5996	925.164
303.15	0.7007	903.304
303.15	0.7991	877.365
303.15	0.8996	844.334
303.15	1.0000	801.964
308.15	0.0000	997.104
308.15	0.1013	988.097
308.15	0.2236	975.701
308.15	0.3036	966.466
308.15	0.4131	951.994
308.15	0.5065	937.569
308.15	0.5996	920.77
308.15	0.7007	898.993
308.15	0.7991	873.162
308.15	0.8996	840.275
308.15	1.0000	798.091
313.15	0.0000	992.481
313.15	0.1013	983.495
313.15	0.2236	971.126
313.15	0.3036	961.914
313.15	0.4131	947.487
313.15	0.5065	933.108
313.15	0.5996	916.363
313.15	0.7007	894.665
313.15	0.7991	868.935
313.15	0.8996	836.188
313.15	1.0000	794.181
318.15	0.0000	987.859
318.15	0.1013	978.879
318.15	0.2236	966.542
318.15	0.3036	957.357
318.15	0.4131	942.969
318.15	0.5065	928.631
318.15	0.5996	911.939
318.15	0.7007	890.317
318.15	0.7991	864.686
318.15	0.8996	832.069
318.15	1.0000	790.229
323.15	0.0000	983.234
323.15	0.1013	974.275
323.15	0.2236	961.962
323.15	0.3036	952.794
323.15	0.4131	938.437
323.15	0.5065	924.136
323.15	0.5996	907.495
323.15	0.7007	885.946
323.15	0.7991	860.406
323.15	0.8996	827.911
323.15	1.0000	786.228
328.15	0.0000	978.613
328.15	0.1013	969.653
328.15	0.2236	957.366
328.15	0.3036	948.222
328.15	0.4131	933.901
328.15	0.5065	919.635
328.15	0.5996	903.036
328.15	0.7007	881.55
328.15	0.7991	856.094
328.15	0.8996	823.712
328.15	1.0000	782.172
333.15	0.0000	973.989
333.15	0.1013	965.036
333.15	0.2236	952.77
333.15	0.3036	943.642
333.15	0.4131	929.347
333.15	0.5065	915.11
333.15	0.5996	898.551
333.15	0.7007	877.126
333.15	0.7991	851.747
333.15	0.8996	819.469
333.15	1.0000	778.056

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1015.63
288.15	0.1013	1006.514
288.15	0.2236	993.986
288.15	0.3036	984.642
288.15	0.4131	969.983
288.15	0.5065	955.349
288.15	0.5996	938.288
288.15	0.7007	916.154
288.15	0.7991	889.873
288.15	0.8996	856.379
288.15	1.0000	813.407
293.15	0.0000	1010.995
293.15	0.1013	1001.909
293.15	0.2236	989.415
293.15	0.3036	980.1
293.15	0.4131	965.493
293.15	0.5065	950.916
293.15	0.5996	933.921
293.15	0.7007	911.881
293.15	0.7991	885.715
293.15	0.8996	852.384
293.15	1.0000	809.621
298.15	0.0000	1006.359
298.15	0.1013	997.307
298.15	0.2236	984.881
298.15	0.3036	975.56
298.15	0.4131	960.897
298.15	0.5065	946.305
298.15	0.5996	929.548
298.15	0.7007	907.599
298.15	0.7991	881.548
298.15	0.8996	848.369
298.15	1.0000	805.804
303.15	0.0000	1001.732
303.15	0.1013	992.702
303.15	0.2236	980.276
303.15	0.3036	971.014
303.15	0.4131	956.499
303.15	0.5065	942.026
303.15	0.5996	925.164
303.15	0.7007	903.304
303.15	0.7991	877.365
303.15	0.8996	844.334
303.15	1.0000	801.964
308.15	0.0000	997.104
308.15	0.1013	988.097
308.15	0.2236	975.701
308.15	0.3036	966.466
308.15	0.4131	951.994
308.15	0.5065	937.569
308.15	0.5996	920.77
308.15	0.7007	898.993
308.15	0.7991	873.162
308.15	0.8996	840.275
308.15	1.0000	798.091
313.15	0.0000	992.481
313.15	0.1013	983.495
313.15	0.2236	971.126
313.15	0.3036	961.914
313.15	0.4131	947.487
313.15	0.5065	933.108
313.15	0.5996	916.363
313.15	0.7007	894.665
313.15	0.7991	868.935
313.15	0.8996	836.188
313.15	1.0000	794.181
318.15	0.0000	987.859
318.15	0.1013	978.879
318.15	0.2236	966.542
318.15	0.3036	957.357
318.15	0.4131	942.969
318.15	0.5065	928.631
318.15	0.5996	911.939
318.15	0.7007	890.317
318.15	0.7991	864.686
318.15	0.8996	832.069
318.15	1.0000	790.229
323.15	0.0000	983.234
323.15	0.1013	974.275
323.15	0.2236	961.962
323.15	0.3036	952.794
323.15	0.4131	938.437
323.15	0.5065	924.136
323.15	0.5996	907.495
323.15	0.7007	885.946
323.15	0.7991	860.406
323.15	0.8996	827.911
323.15	1.0000	786.228
328.15	0.0000	978.613
328.15	0.1013	969.653
328.15	0.2236	957.366
328.15	0.3036	948.222
328.15	0.4131	933.901
328.15	0.5065	919.635
328.15	0.5996	903.036
328.15	0.7007	881.55
328.15	0.7991	856.094
328.15	0.8996	823.712
328.15	1.0000	782.172
333.15	0.0000	973.989
333.15	0.1013	965.036
333.15	0.2236	952.77
333.15	0.3036	943.642
333.15	0.4131	929.347
333.15	0.5065	915.11
333.15	0.5996	898.551
333.15	0.7007	877.126
333.15	0.7991	851.747
333.15	0.8996	819.469
333.15	1.0000	778.056

Sources

• Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME